JP4696516B2 - Pre-treatment method for electrodeposition coating - Google Patents

Pre-treatment method for electrodeposition coating Download PDF

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JP4696516B2
JP4696516B2 JP2004288197A JP2004288197A JP4696516B2 JP 4696516 B2 JP4696516 B2 JP 4696516B2 JP 2004288197 A JP2004288197 A JP 2004288197A JP 2004288197 A JP2004288197 A JP 2004288197A JP 4696516 B2 JP4696516 B2 JP 4696516B2
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electrodeposition coating
water washing
coated
alkaline
chemical conversion
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JP2006097120A (en
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重徳 風間
修 田中
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Nissan Motor Co Ltd
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本発明は、自動車ボディや部品の電着塗装の表面処理方法に関し、特に化成皮膜を形成した後の筋錆や電着二次タレを防止できる前処理方法に関する。   The present invention relates to a surface treatment method for electrodeposition coating of automobile bodies and parts, and more particularly to a pretreatment method capable of preventing muscle rust and electrodeposition secondary sagging after forming a chemical conversion film.

自動車ボディの電着前処理工程は、脱脂、水洗、表面調整、化成処理、水洗、純水洗、水切り乾燥といった工程で構成され、この後に電着塗装、水洗、焼付け乾燥の各工程を経て電着塗膜が形成される(特許文献1)。   The pre-electrodeposition treatment process for automobile bodies consists of steps such as degreasing, water washing, surface conditioning, chemical conversion treatment, water washing, pure water washing and draining and drying, followed by electrodeposition coating, water washing and baking drying. A coating film is formed (Patent Document 1).

こうした前処理工程において、化成処理後に上水を用いた水洗工程と純水を用いた純水洗工程によってボディ表面に付着した化成処理液を除去しているが、この水洗が不充分であると、ボディのパネル合わせ面などの狭隘部や外板部に前処理液が残留し、この前処理液が酸性であることから錆が発生する。したがって、水洗と純水洗は前処理液が残留しないように充分に行う必要があり、多量の上水及び純水を消費するという問題があった。   In such a pretreatment step, the chemical conversion treatment liquid adhering to the body surface is removed by a water washing step using clean water and a pure water washing step using pure water after the chemical conversion treatment, but if this water washing is insufficient, The pretreatment liquid remains in the narrow part and the outer plate part such as the panel mating surface of the body, and rust is generated because the pretreatment liquid is acidic. Therefore, it is necessary to perform washing with water and pure water sufficiently so that the pretreatment liquid does not remain, and there is a problem that a large amount of clean water and pure water are consumed.

また、水洗及び純水洗後にボディを長時間放置すると、ボディに付着した前処理液が乾燥して濃縮され、これが乾きムラ(斑)と称される筋状の錆(以下、筋錆ともいう。) の不具合となる。したがって、前処理工程と電着工程との間はできる限り短時間で通過させるように設計する必要があるが、こうした筋錆の発生を防止するためには、電着塗装後のラインが停止したときに前処理を終了したボディを暫定的に退避させるストレージラインを設置しなければならなかった。非常時のためのストレージラインの設置は、設備費用だけでなく広いスペースが必要となるので工程設計をする上でネックとなっていた。   Further, when the body is left for a long time after washing with water and pure water, the pretreatment liquid adhering to the body is dried and concentrated, and this is dried to cause streak rust (hereinafter referred to as muscle rust). ). Therefore, it is necessary to design between the pretreatment process and the electrodeposition process as quickly as possible, but in order to prevent the occurrence of such rust, the line after electrodeposition coating stopped. Sometimes it was necessary to install a storage line to temporarily evacuate the body after preprocessing. Installation of storage lines for emergencies has become a bottleneck in process design because it requires not only equipment costs but also a large space.

さらに、前処理液がボディの狭隘部などに残留すると、電着塗装後の焼付け工程で濃縮されて強酸性水となり、これが未乾燥の電着塗膜を侵して二次タレが発生するといった問題もあった。
特開平10−46393号公報
Furthermore, if the pretreatment liquid remains in the narrow part of the body, it is concentrated in the baking process after electrodeposition coating to become strongly acidic water, which erodes the undried electrodeposition coating film and causes secondary sagging. There was also.
Japanese Patent Laid-Open No. 10-46393

本発明は、化成皮膜を形成した後の筋錆や電着二次タレを防止できる前処理方法を提供することを目的とする。
上記目的を達成するために、本発明によれば、被塗物の表面に電着塗膜を形成する電着塗装工程前の前処理方法であって、前記被塗物の表面に化成皮膜を形成する化成処理工程と、アルカリ性電解水を主成分とするアルカリ性水溶液を用いて前記被塗物を洗浄するアルカリ水洗工程と、を有することを特徴とする電着塗装の前処理方法が提供される。
An object of this invention is to provide the pre-processing method which can prevent the muscle rust and electrodeposition secondary sagging after forming a chemical conversion film.
In order to achieve the above object, according to the present invention, there is provided a pretreatment method prior to an electrodeposition coating process for forming an electrodeposition coating film on the surface of an object to be coated, wherein a chemical conversion film is formed on the surface of the object to be coated. There is provided a pretreatment method for electrodeposition coating, comprising: a chemical conversion treatment step to be formed; and an alkaline water washing step for washing the object to be coated using an alkaline aqueous solution mainly composed of alkaline electrolyzed water. .

本発明では、化成処理工程の後にアルカリ性電解水を主成分とするアルカリ性水溶液を用いて被塗物を洗浄するので、被塗物が電着塗装工程前に長時間放置されても被塗物の残留水が酸性側に濃縮されることがなくなり、筋錆等の錆の発生を防止することができる。 In the present invention, after the chemical conversion treatment step, the coated object is washed with an alkaline aqueous solution mainly composed of alkaline electrolyzed water. Therefore, even if the coated material is left for a long time before the electrodeposition coating process, Residual water is not concentrated on the acidic side, and generation of rust such as muscle rust can be prevented.

また、化成処理工程の後にアルカリ性電解水を主成分とするアルカリ性水溶液を用いて被塗物を洗浄するので、被塗物の狭隘部などに残留したアルカリ性水溶液によって電着塗装の通電前に電着塗膜が析出し、これにより狭隘部などに過剰な電着塗料液が浸入するのを抑制することができる。その結果、電着焼付け後に生じる二次タレを防止することができる。 In addition, since the article to be coated is washed with an alkaline aqueous solution mainly composed of alkaline electrolyzed water after the chemical conversion treatment step, the electrodeposition is performed before the electrodeposition coating is energized by the alkaline aqueous solution remaining in the narrow part of the article to be coated. A coating film is deposited, which can prevent an excessive electrodeposition coating liquid from penetrating into a narrow portion or the like. As a result, secondary sagging that occurs after electrodeposition baking can be prevented.

発明の実施の形態BEST MODE FOR CARRYING OUT THE INVENTION

以下、本発明の実施形態を図面に基づいて説明する。
図1は、本発明に係る電着塗装の前処理方法を用いた自動車ボディの塗装ライン(前処理〜電着塗装・焼付)までの工程の一実施形態を示す工程図、図2はこのうちの表面処理工程〜水切り乾燥工程までの前処理装置を概略的に示す図である。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a process diagram showing an embodiment of a process from an automobile body coating line (pretreatment to electrodeposition coating / baking) using the electrodeposition coating pretreatment method according to the present invention, and FIG. It is a figure which shows roughly the pre-processing apparatus from a surface treatment process of-to a draining drying process.

図1に示すように、本例の前処理ラインは、脱脂工程1、水洗工程2、表面調整工程3、化成処理工程4、水洗工程5、アルカリ水洗工程6、水切り乾燥工程7から構成され、この後に電着塗装工程8、水洗工程9、焼付け工程10が設けられている。   As shown in FIG. 1, the pretreatment line of this example is composed of a degreasing process 1, a water washing process 2, a surface conditioning process 3, a chemical conversion treatment process 4, a water washing process 5, an alkaline water washing process 6, and a draining and drying process 7. After this, an electrodeposition coating process 8, a water washing process 9, and a baking process 10 are provided.

なお、本例に係る前処理方法はアルカリ水洗工程6であることから、脱脂工程1〜水洗工程5、及び水切り乾燥工程7〜焼付け工程10までの各工程に関しては、特に制限されるものでなく、既知の製造技術(製造方法、直接・間接材料、製造装置・設備等を含む)を広く適用することができる。そのため、本例の前処理方法を採用するにあたっては、アルカリ水洗工程6の前工程である脱脂工程1〜水洗工程5と、アルカリ水洗工程6の後工程である水切り乾燥工程7〜焼付け工程10までの工程に関し既存の塗装ラインをそのまま適用することができる。すなわち、水洗工程5と水切り乾燥工程7の間に純水洗工程を有する既存設備を改造する場合にあっては、純水洗工程を本例に係るアルカリ水洗工程6に変更するだけで本発明の効果を充分に発揮することができる。   In addition, since the pre-processing method which concerns on this example is the alkaline water washing process 6, it does not restrict | limit in particular about each process from the degreasing process 1-the water washing process 5 and the draining drying process 7-the baking process 10. The known manufacturing techniques (including manufacturing methods, direct / indirect materials, manufacturing apparatus / equipment, etc.) can be widely applied. Therefore, in adopting the pretreatment method of this example, from the degreasing process 1 to the water washing process 5 which is a pre-process of the alkaline water washing process 6 and the draining and drying process 7 to the baking process 10 which is a subsequent process of the alkaline water washing process 6. The existing coating line can be applied as it is for this process. That is, when remodeling an existing facility having a pure water washing step between the water washing step 5 and the draining and drying step 7, the effect of the present invention can be obtained only by changing the pure water washing step to the alkaline water washing step 6 according to this example. Can be fully exhibited.

脱脂工程1は、自動車ボディを強アルカリタイプの脱脂剤、たとえばカセイソーダおよび界面活性剤が40〜60℃程度に保持されて満たされた脱脂槽に2〜3分間浸漬させ、自動車ボディに付着した油分及び塵埃を除去する工程である。   In the degreasing step 1, the automobile body is immersed in a degreasing tank filled with a strong alkaline type degreasing agent such as caustic soda and a surfactant held at about 40 to 60 ° C. for 2 to 3 minutes. And a step of removing dust.

脱脂工程1に続く水洗工程2は、常温の上水をたとえば約20秒間、自動車ボディにスプレー噴霧し、ボディ表面に付着した脱脂剤を洗浄する工程である。この水洗工程は、必要に応じて複数段、たとえば2回(2工程)行う。     The water washing step 2 following the degreasing step 1 is a step of spraying normal temperature clean water onto the automobile body for about 20 seconds, for example, to wash the degreasing agent adhering to the body surface. This water washing step is performed in a plurality of stages, for example, twice (two steps) as necessary.

水洗工程2に続く表面調整工程3は、自動車ボディを、表面調整剤(たとえば、日本ペイント社製サーフファイン5N−10)が室温に保持されて満たされた表面調整槽31(図2参照)に約20秒間浸漬させ、ボディ表面にリン酸亜鉛結晶のための結晶核を作る工程である。     In the surface conditioning step 3 following the water washing step 2, the automobile body is placed in a surface conditioning tank 31 (see FIG. 2) filled with a surface conditioning agent (for example, Surf Fine 5N-10 manufactured by Nippon Paint Co., Ltd.) held at room temperature. This is a step of immersing for about 20 seconds to form crystal nuclei for zinc phosphate crystals on the body surface.

表面調整工程3に続く化成処理工程4は、自動車ボディを、リン酸亜鉛系化成処理液が40〜50℃に保持されて満たされた化成槽41(図2参照)に2〜3分間浸漬させ、ボディ表面に約3〜10μm(焼付後の厚み)のリン酸亜鉛被膜を形成する工程である。     In the chemical conversion treatment step 4 following the surface conditioning step 3, the automobile body is immersed in a chemical conversion bath 41 (see FIG. 2) filled with a zinc phosphate-based chemical conversion treatment solution held at 40 to 50 ° C. for 2 to 3 minutes. This is a step of forming a zinc phosphate coating of about 3 to 10 μm (thickness after baking) on the body surface.

化成処理工程4に続く水洗工程5は、自動車ボディに、常温の上水をノズル51(図2参照)から約20秒間スプレー噴霧し、自動車ボディに付着した化成処理液を洗浄する工程である。この水洗工程5は必要に応じて複数段、たとえば2〜3回行う。図2において、水洗に用いた上水は回収タンク52で回収したのち、ノズル51から噴霧する。     The water washing step 5 following the chemical conversion treatment step 4 is a step of washing the chemical conversion treatment liquid adhering to the automobile body by spraying normal temperature clean water from the nozzle 51 (see FIG. 2) for about 20 seconds onto the automobile body. This water washing step 5 is performed in a plurality of stages, for example, 2 to 3 times as necessary. In FIG. 2, clean water used for washing is collected in the collection tank 52 and then sprayed from the nozzle 51.

また、スプレー噴霧に加えて又はこれに代えて常温の上水が満たされた水槽に自動車ボディを約20秒間浸漬させるディップ式洗浄装置であっても良い。なお、化成処理液の残留状態が良好、あるいは化成処理液が残留していても問題の生じない化成処理液を用いた場合には、この洗浄工程5を省略し、化成処理工程4に続けて次のアルカリ水洗工程6を直接設けても良い。   Further, in addition to or instead of spraying, a dip-type cleaning device that immerses the automobile body in a water tank filled with clean water at room temperature for about 20 seconds may be used. In addition, when the chemical conversion treatment liquid is used in a good state or a chemical conversion treatment liquid that does not cause a problem even if the chemical conversion treatment liquid remains, this cleaning step 5 is omitted, and the chemical conversion treatment step 4 is continued. The next alkaline water washing step 6 may be provided directly.

本例では、水洗工程5の後に純水を用いた水洗工程を設けず、これに代えてアルカリ性水溶液を用いて自動車ボディを洗浄するアルカリ水洗工程6を設けている。化成処理工程4を終えた自動車ボディ表面はpHが4前後の酸性になっているが、このアルカリ水洗工程6においてアルカリ性水溶液で洗浄することによりボディ表面が中性〜アルカリ性に移行し、これにより電着塗装工程8の前にボディを長時間放置しても筋錆の発生を抑制することができる。また、二次タレの発生も抑制することができる。   In this example, the water-washing process using pure water is not provided after the water-washing process 5, but instead, an alkaline water-washing process 6 for washing the automobile body using an alkaline aqueous solution is provided. The surface of the automobile body that has undergone the chemical conversion treatment step 4 is acidic at a pH of around 4. However, by washing with an alkaline aqueous solution in this alkaline water washing step 6, the body surface changes from neutral to alkaline. Even if the body is left for a long time before the coating process 8, the generation of muscle rust can be suppressed. Also, the occurrence of secondary sagging can be suppressed.

アルカリ水洗工程6で用いられるアルカリ性水溶液としては、水酸化アンモニウムまたは有機塩基を含有する水溶液や、アルカリ性電解水を例示することができ、特に水洗後の後処理(排水処理など)が容易であることや化成皮膜に対する影響が少ないことから、本例に係るアルカリ性水溶液としてアルカリ性電解水が最も好ましい。     Examples of the alkaline aqueous solution used in the alkaline water washing step 6 include aqueous solutions containing ammonium hydroxide or an organic base and alkaline electrolyzed water, and particularly easy post-treatment (such as wastewater treatment) after washing with water. Alkaline electrolyzed water is most preferable as the alkaline aqueous solution according to this example because it has little influence on the chemical conversion film.

また、アルカリ水洗工程6で用いられるアルカリ性水溶液のpHは、8〜12であることが好ましい。pHが8未満であると本発明の効果が少なく、またpHが12を超えると化成皮膜が再溶解するおそれがある。   The pH of the alkaline aqueous solution used in the alkaline water washing step 6 is preferably 8-12. If the pH is less than 8, the effect of the present invention is small, and if the pH exceeds 12, the chemical conversion film may be redissolved.

また、本例のアルカリ水洗工程6は、図2に示すようにアルカリ性水溶液を満たした水槽61に自動車ボディを浸漬させるディップ方式であっても、上述した水洗工程5のようなスプレー方式であっても特に制限されるものでない。ただし、ボディのパネル合わせ面にアルカリ性水溶液を浸入させ易いことから言えばディップ式が望ましいが、既存の塗装ラインに適用されている方式を用いるのも設備費用の点からは有利である。   Moreover, even if the alkaline water washing process 6 of this example is a dip system which immerses a motor vehicle body in the water tank 61 filled with alkaline aqueous solution as shown in FIG. 2, it is a spray system like the water washing process 5 mentioned above. Is not particularly limited. However, the dip type is desirable because it is easy to allow the alkaline aqueous solution to enter the panel mating surface of the body, but it is advantageous from the viewpoint of the equipment cost to use the method applied to the existing coating line.

アルカリ性水溶液を用いた洗浄時間およびアルカリ性水溶液の温度に関しても、特に制限されるものでないが、本例ではボディ表面にアルカリ性水溶液を付着させれば足りることから、ディップ方式では20秒前後浸漬されれば良い。   The washing time using the alkaline aqueous solution and the temperature of the alkaline aqueous solution are not particularly limited, but in this example, it is sufficient to attach the alkaline aqueous solution to the body surface. good.

アルカリ水洗工程6に続く水切り乾燥工程7は、自動車ボディを水切り乾燥炉71に搬入し、100〜130℃で10〜15分間加熱する。この水切り乾燥工程7に関しても特に制限されるものでなく、一般的な製造ラインをはじめとする既知の製造技術(乾燥方法、乾燥装置・設備等を含む)を広く適用することができる。アルカリ性水溶液がボディに付着したまま電着塗装を行うと、電着槽に局所的な濃度差が生じ、これにより電着ムラが発生するため、この水切り乾燥工程7でボディ表面のアルカリ性水溶液を蒸発させるが、この工程は蒸発させれば足りる処理であることから、アルカリ性水溶液の付着状況によって水切り乾燥工程7を省略することもできる。   In the draining and drying step 7 following the alkaline water washing step 6, the automobile body is carried into the draining and drying furnace 71 and heated at 100 to 130 ° C. for 10 to 15 minutes. The draining and drying process 7 is not particularly limited, and a wide range of known manufacturing techniques (including a drying method, a drying apparatus / equipment, etc.) including a general manufacturing line can be widely applied. If electrodeposition coating is performed with the alkaline aqueous solution attached to the body, a local concentration difference occurs in the electrodeposition tank, resulting in uneven electrodeposition. This causes the alkaline aqueous solution on the body surface to evaporate in this draining and drying step 7. However, since this process is sufficient if it is evaporated, the draining and drying process 7 can be omitted depending on the state of attachment of the alkaline aqueous solution.

なお、水切り乾燥工程7を終えた自動車ボディは、アルカリ性水溶液による処理によってアルカリ性になっており、発錆のおそれがないために暫定退避するためのストレージラインは不要である。   The automobile body that has finished the draining and drying step 7 is made alkaline by the treatment with the alkaline aqueous solution, and there is no risk of rusting, so a storage line for temporary retraction is unnecessary.

以上の前処理を行った後、電着塗装工程8、水洗工程9、焼付け乾燥工程10の各工程を経て電着塗膜が形成される。これら電着塗装8〜焼付け乾燥10までの各工程に関しては特に制限されるものでなく、一般的な塗装ラインをはじめとする既知の製造技術(製造方法、直接・間接材料、製造装置・設備等を含む)を広く適用することができるため、既存の塗装ラインをそのまま適用することもできる。     After performing the above pretreatment, an electrodeposition coating film is formed through each process of the electrodeposition coating process 8, the water washing process 9, and the baking drying process 10. These processes from electrodeposition coating 8 to baking drying 10 are not particularly limited, and are known manufacturing techniques (manufacturing methods, direct / indirect materials, manufacturing equipment / equipment, etc.) including general coating lines. Can be applied widely, so existing coating lines can be applied as they are.

電着塗装8〜焼付け乾燥10までの工程の一例を説明すると、前処理を終了した自動車ボディは、そのまま電着塗装工程8に搬送される。この電着塗装工程8は、防錆を主目的としてボディ鋼板の表裏全面を塗装するもので、高防錆力が得られるカチオン電着塗料(例えば、ブロックイソシアネート変性エポキシ系)が満たされた電着槽にボディを浸漬させる。電着塗料は、塗料温度が25〜30℃の範囲になるように電着槽内で±1℃に保持され、たとえば塗装時間が2〜5分間、電圧は150〜300V、電流は2000Aなどの塗装条件でカチオン電着が行われる。     If an example of the process from the electrodeposition coating 8 to baking drying 10 is demonstrated, the motor vehicle body which finished the pre-processing will be conveyed to the electrodeposition coating process 8 as it is. This electrodeposition coating process 8 is for coating the entire front and back surfaces of the body steel plate for the purpose of rust prevention. The electrodeposition coating process (for example, blocked isocyanate-modified epoxy system) that provides high rust-preventing power is satisfied. Immerse the body in the tank. The electrodeposition paint is held at ± 1 ° C. in the electrodeposition tank so that the paint temperature is in the range of 25-30 ° C., for example, the coating time is 2-5 minutes, the voltage is 150-300V, the current is 2000A, etc. Cationic electrodeposition is performed under coating conditions.

電着塗装工程8に続く水洗工程9では、常温の上水を約20秒間スプレー噴霧して自動車ボディの濾液水洗を行った後、上水が満たされた水槽にボディを約20秒間浸漬させて水洗し、さらに常温の上水を約20秒間スプレー噴霧して洗浄する。これにより、ボディの電着塗膜表面に付着している未反応電着塗料を除去する。     In the water washing step 9 following the electrodeposition coating step 8, normal water is sprayed for about 20 seconds to wash the filtrate of the automobile body, and the body is immersed in a water tank filled with water for about 20 seconds. Wash with water, and spray with normal temperature water for about 20 seconds. Thereby, the unreacted electrodeposition paint adhering to the electrodeposition coating film surface of the body is removed.

水洗工程9に続く焼付け工程10では、ボディの電着塗膜(ウェット状態)を150〜170℃で15〜30分間焼付け、膜厚が20〜30μmの乾燥した電着塗膜を形成する。   In the baking process 10 following the water washing process 9, the electrodeposition coating film (wet state) of the body is baked at 150 to 170 ° C. for 15 to 30 minutes to form a dried electrodeposition coating film having a film thickness of 20 to 30 μm.

以上が前処理〜電着塗装に至る本例の工程概要であるが、本例のアルカリ性水溶液によるアルカリ水洗工程6によって、電着二次タレの発生が抑制できる点について説明する。   The above is the outline of the process of this example from pretreatment to electrodeposition coating, but the point that the electrodeposition secondary sagging can be suppressed by the alkaline water washing process 6 using the alkaline aqueous solution of this example will be described.

電着二次タレとは、鋼板合わせ目の内部に残留した電着塗料液が、水洗工程9による洗浄によっても抜けきらず、その後の焼付け工程10の入口側においてボディ温度が100℃以上の高温になったときにこの鋼板合わせ目から突沸し、外板面の未硬化塗膜を侵しながら硬化して塗膜表面に凹凸を生じさせる塗装不具合をいう。そして、この電着二次タレ不具合は、鋼板合わせ目付近の塗装仕上がり外観を損なうものであり、その外観修正に多大の工数がかかってしまう。たとえば、図3(A)に示すように、サイドシル50とセンターピラー60との接続部Bは、同図(B)および図4に示されるように、サイドシルアウタパネル51とセンターピラーアウタパネル61とがいわゆるベタ当たりする構造であり、表面張力によってベタ当たり面Dの隙間に浸入した電着塗料液が焼付け炉内で噴き出し、これがシルアウタに垂れ流れて、場合によっては図5に示すように広い範囲で硬化する。   The electrodeposition secondary sagging means that the electrodeposition coating liquid remaining inside the steel sheet joint cannot be removed even by washing in the water washing step 9, and the body temperature reaches a high temperature of 100 ° C. or higher on the inlet side of the subsequent baking step 10. When this happens, it means a coating failure that bumps from the joint of the steel plates and hardens while corroding the uncured coating on the outer plate surface to cause irregularities on the coating surface. This electrodeposition secondary sagging defect impairs the appearance of the finished paint near the joint of the steel plates, and it takes a lot of man-hours to correct the appearance. For example, as shown in FIG. 3 (A), the connecting portion B between the side sill 50 and the center pillar 60 has a so-called side sill outer panel 51 and center pillar outer panel 61 as shown in FIG. It is a solid-contact structure, and the electrodeposition coating liquid that has entered the gap between the solid-contact surfaces D due to surface tension is sprayed in the baking furnace and flows down to the silouter. To do.

本例の前処理方法では、アルカリ水洗工程6にてアルカリ性水溶液を用いてボディを洗浄するので、特にディップ式によるアルカリ水洗処理を行うことで、こうしたボディの鋼板合わせ面にもアルカリ性水溶液が浸入する。このアルカリ性水溶液は鋼板合わせ面に残留するが、このアルカリ性水溶液によって弱酸性塗料を用いる電着塗装の通電前、すなわちボディが電着槽に入槽したときに鋼板合わせ面に電着塗膜が析出する。これにより鋼板合わせ面に過剰な電着塗料液が浸入するのを抑制することができ、その結果、電着焼付け後に生じる二次タレを防止することができる。   In the pretreatment method of this example, the body is washed with an alkaline aqueous solution in the alkaline water washing step 6, and thus the alkaline aqueous solution infiltrates also into the steel sheet mating surface of the body by performing the alkaline water washing treatment by the dip method. . This alkaline aqueous solution remains on the mating surface of the steel sheet, but the electrodeposition coating film is deposited on the mating surface of the steel plate before energization of the electrodeposition coating using the weakly acidic paint by this alkaline aqueous solution, that is, when the body enters the electrodeposition bath. To do. Thereby, it can suppress that an excessive electrodeposition coating liquid penetrate | invades into a steel plate mating surface, As a result, the secondary sagging produced after electrodeposition baking can be prevented.

なお、以上説明した実施形態は、本発明の理解を容易にするために記載されたものであって、本発明を限定するために記載されたものではない。したがって、上記の実施形態に開示された各要素は、本発明の技術的範囲に属する全ての設計変更や均等物をも含む趣旨である。   The embodiment described above is described for facilitating the understanding of the present invention, and is not described for limiting the present invention. Therefore, each element disclosed in the above embodiment is intended to include all design changes and equivalents belonging to the technical scope of the present invention.

本発明の実施形態に係る前処理方法を示す工程図である。It is process drawing which shows the pre-processing method which concerns on embodiment of this invention. 本発明の実施形態に係る前処理方法を適用した塗装ライン要部の前処理装置を概略的に示す図である。It is a figure which shows roughly the pre-processing apparatus of the coating line principal part to which the pre-processing method which concerns on embodiment of this invention is applied. (A)は被塗物である自動車ボディを示す斜視図、(B)はB部の拡大図である。(A) is a perspective view which shows the motor vehicle body which is a to-be-coated object, (B) is an enlarged view of the B section. 図3(B)のC−C線に沿う断面概略図である。FIG. 4 is a schematic cross-sectional view taken along line CC in FIG. 3 (B). 図4のE矢視図であって、車体サイドの鋼板合わせ目部(センターピラーとサイドシルの合わせ目部)より流出した塗料液による焼付け後のタレ跡を模式的に表した図である。FIG. 5 is a diagram schematically showing a sagging trace after baking with a coating liquid flowing out from a steel plate joint portion (a center pillar and a side sill joint portion) on the vehicle body side, as viewed from the arrow E in FIG. 4.

符号の説明Explanation of symbols

1…脱脂工程
2…水洗工程
3…表面調整工程
4…化成処理工程
5…水洗工程
6…アルカリ水洗工程
7…水切り乾燥工程
8…電着塗装工程
9…水洗工程
10…焼付け工程

DESCRIPTION OF SYMBOLS 1 ... Degreasing process 2 ... Water washing process 3 ... Surface adjustment process 4 ... Chemical conversion treatment process 5 ... Water washing process 6 ... Alkaline water washing process 7 ... Draining drying process 8 ... Electrodeposition coating process 9 ... Water washing process 10 ... Baking process

Claims (9)

被塗物の表面に電着塗膜を形成する電着塗装工程前の前処理方法であって、
前記被塗物の表面に化成皮膜を形成する化成処理工程と、
アルカリ性電解水を主成分とするアルカリ性水溶液を用いて前記被塗物を洗浄するアルカリ水洗工程と、
を有することを特徴とする電着塗装の前処理方法。
A pretreatment method before an electrodeposition coating process for forming an electrodeposition coating on the surface of an object to be coated,
A chemical conversion treatment step for forming a chemical conversion film on the surface of the object to be coated;
An alkaline water washing step of washing the object to be coated using an alkaline aqueous solution mainly composed of alkaline electrolyzed water ;
A pretreatment method for electrodeposition coating, comprising:
前記化成処理工程と前記アルカリ水洗工程の間に、上水を用いて前記被塗物を洗浄する水洗工程を有することを特徴とする請求項1記載の電着塗装の前処理方法。   The pretreatment method for electrodeposition coating according to claim 1, further comprising a water washing step of washing the object to be coated using clean water between the chemical conversion treatment step and the alkaline water washing step. 前記化成処理工程の前に、脱脂液を用いて前記被塗物を洗浄する脱脂洗浄工程を有することを特徴とする請求項1又は2記載の電着塗装の前処理方法。   3. The pretreatment method for electrodeposition coating according to claim 1 or 2, further comprising a degreasing cleaning step of cleaning the object to be coated using a degreasing liquid before the chemical conversion treatment step. 前記アルカリ水洗工程と前記電着塗装工程の間に、前記被塗物を乾燥させる乾燥工程を有することを特徴とする請求項1〜3の何れかに記載の電着塗装の前処理方法。   The pretreatment method for electrodeposition coating according to any one of claims 1 to 3, further comprising a drying step of drying the object to be coated between the alkaline water washing step and the electrodeposition coating step. 前記アルカリ性水溶液のpHは、8〜12であることを特徴とする請求項1〜の何れかに記載の電着塗装の前処理方法。 The pretreatment method for electrodeposition coating according to any one of claims 1 to 4 , wherein the pH of the alkaline aqueous solution is 8 to 12. 前記アルカリ水洗工程は、前記アルカリ性水溶液に前記被塗物を浸漬させて洗浄することを特徴とする請求項1〜の何れかに記載の電着塗装の前処理方法。 The pretreatment method for electrodeposition coating according to any one of claims 1 to 5 , wherein the alkaline water washing step is performed by immersing the article to be coated in the alkaline aqueous solution. 前記化成処理工程と電着塗装工程との間に、純水を用いて前記被塗物を洗浄する工程を有しないことを特徴とする請求項1〜の何れかに記載の電着塗装の前処理方法。 The electrodeposition coating process according to any one of claims 1 to 6 , wherein there is no step of washing the object to be coated with pure water between the chemical conversion treatment step and the electrodeposition coating step. Pre-processing method. 前記化成処理工程が、リン酸亜鉛系化成処理液を用いて前記被塗物表面に化成皮膜を形成することを特徴とする請求項1〜の何れかに記載の電着塗装の前処理方法。 The chemical conversion treatment step, the pretreatment method for electrodeposition coating according to any one of claims 1 to 7, characterized in that to form a conversion coating on the coating object surface with a zinc phosphate conversion treatment solution . 前記電着塗装工程が、カチオン系電着塗料を用いて前記被塗物表面に電着塗膜を形成することを特徴とする請求項1〜の何れかに記載の電着塗装の前処理方法。 The electrodeposition coating pretreatment according to any one of claims 1 to 8 , wherein the electrodeposition coating step forms an electrodeposition coating film on the surface of the object to be coated using a cationic electrodeposition coating. Method.
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JPS60100696A (en) * 1983-11-07 1985-06-04 Nippon Paint Co Ltd Method for temporarily preventing rust before coating by electrodeposition
JPH04365897A (en) * 1991-02-25 1992-12-17 Kansai Paint Co Ltd Method for forming corrosion preventing coating film

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60100696A (en) * 1983-11-07 1985-06-04 Nippon Paint Co Ltd Method for temporarily preventing rust before coating by electrodeposition
JPH04365897A (en) * 1991-02-25 1992-12-17 Kansai Paint Co Ltd Method for forming corrosion preventing coating film

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