JP4862484B2 - Method for producing electrogalvanized steel sheet - Google Patents
Method for producing electrogalvanized steel sheet Download PDFInfo
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Description
この発明は、白色度の高い外観を有する電気亜鉛めっき鋼板の製造方法に関する。 The present invention relates to a method for producing an electrogalvanized steel sheet having an appearance with high whiteness.
電気亜鉛めっき鋼板は家電製品、自動車、建材等の広範な用途で使用されている。近年、無塗装で使用される家電用途向け各種化成処理電気亜鉛めっき鋼板の需要が増大しており、重要な用途分野となっている。この用途では無塗装で使用されるために表面外観に優れることが要求される。優れた表面外観の条件としては、ムラ等の表面欠陥が無いことに加え、白色度が高いことが要求される。各種化成処理後の外観は化成処理前の亜鉛めっきの外観に大きく左右されるため、白色度が高い電気亜鉛めっき鋼板を得ることのできる製造技術が求められてきた。 Electrogalvanized steel sheets are used in a wide range of applications such as home appliances, automobiles, and building materials. In recent years, the demand for various types of chemically treated electrogalvanized steel sheets for home appliances used without coating has increased, and this has become an important application field. In this application, since it is used without coating, it is required to have an excellent surface appearance. Excellent surface appearance conditions require high whiteness in addition to no surface defects such as unevenness. Since the appearance after various chemical conversion treatments is greatly influenced by the appearance of galvanization before chemical conversion treatment, a production technique capable of obtaining an electrogalvanized steel sheet having high whiteness has been demanded.
めっき鋼板の白色度を向上させる方法として、めっき浴に無機イオンを添加する方法がある(例えば、特許文献1)。 As a method for improving the whiteness of the plated steel sheet, there is a method of adding inorganic ions to the plating bath (for example, Patent Document 1).
また、別の方法として、めっき浴中に有機物を添加する方法がある。特許文献2では、グリシン、アスパラギン酸、カルボン酸基を2つ以上有するカルボン酸またはその塩の群から選択された1種又は2種をめっき浴中に添加する方法が開示されている。特許文献3では、電気亜鉛めっき浴添加剤として、ナフテン酸の金属塩、アニリン誘導体、低級アルカノイル化合物、及び有機過酸化物よりなる群から選択される少なくとも1種が開示されている。 Another method is to add an organic substance to the plating bath. Patent Document 2 discloses a method in which one or two selected from the group of glycine, aspartic acid, a carboxylic acid having two or more carboxylic acid groups, or a salt thereof is added to the plating bath. Patent Document 3 discloses at least one selected from the group consisting of a metal salt of naphthenic acid, an aniline derivative, a lower alkanoyl compound, and an organic peroxide as an electrogalvanizing bath additive.
また、特許文献4では、可溶性のイオウ含有有機化合物を含有する酸性浴中で陰極電解し、引き続き、りん酸亜鉛処理する方法が開示されている。
しかしながら、上記特許文献には以下の問題点がある。
特許文献1においては、めっき浴に無機物を添加する方法であるため、めっき皮膜中に無機物が共析し、共析によりめっき皮膜の耐食性が劣化したり外観が急激に変化して光沢化してしまう。
However, the above patent document has the following problems.
In patent document 1, since it is the method of adding an inorganic substance to a plating bath, an inorganic substance co-deposits in a plating film, and the corrosion resistance of the plating film deteriorates due to the eutectoid or the appearance rapidly changes to become glossy. .
特許文献2および3では、白色度の上昇に伴い光沢度が上昇したり、めっき電流効率の低下により製造コストアップを招くなどの問題がある。 In Patent Documents 2 and 3, there is a problem that the glossiness increases with an increase in whiteness and a manufacturing cost increases due to a decrease in plating current efficiency.
特許文献4では、めっきの光沢度を上昇させ、緻密で平滑なりん酸亜鉛皮膜を形成させてりん酸亜鉛処理後のL値を高くするための技術である。即ち、りん酸亜鉛処理による白色度の低下が8未満と小さいことに特徴がある。しかし、めっき後の外観については、光沢度は上昇するが、白色度を上昇させる効果はない。 In patent document 4, it is the technique for raising the glossiness of metal plating, forming a precise | minute and smooth zinc phosphate film, and raising the L value after a zinc phosphate process. That is, the reduction in whiteness due to the zinc phosphate treatment is as small as less than 8. However, with regard to the appearance after plating, the glossiness increases, but there is no effect of increasing the whiteness.
このように、従来の方法では、いずれもめっきの白色度の上昇効果が不十分である。また、白色度を上昇させることはできても耐食性低下、光沢化等、他の特性が大きく変化してしまう、あるいは電流効率が大きく低下してしまうといった問題がある。 As described above, any of the conventional methods is insufficient in increasing the whiteness of the plating. In addition, even if the whiteness can be increased, other characteristics such as a decrease in corrosion resistance and glossing are greatly changed, or the current efficiency is greatly decreased.
本発明は、上記の事情に鑑み、光沢度を大きく変化させずに、また、電流効率を大きく低下させずに、高い白色度を有する電気亜鉛めっき鋼板を製造する方法を提供することを目的とする。 In view of the above circumstances, the present invention has an object to provide a method for producing an electrogalvanized steel sheet having high whiteness without greatly changing glossiness and without greatly reducing current efficiency. To do.
本発明者らが高い白色度を有する電気亜鉛めっき鋼板の製造方法を開発する為、研究を重ねた結果、メルカプト基(−SH)を有する有機化合物の1種又は2種以上を合計で0.5〜30mg/l含有する電気亜鉛めっき浴中で、電解を5回以上に分割して行うとともに、前記各々の電解の間に、鋼板を前記酸性めっき浴中に0.2秒以上浸漬することにより、高い白色度を有する電気亜鉛めっき鋼板を製造できることを見出した。従来、めっき浴中に有機化合物を添加する方法では、外観の光沢化、電流効率の低下、あるいはアノード寿命の短縮といった弊害が一般には不可避であるが、本方法では非常に低い添加濃度で白色化効果が得られる為、上述した弊害を招かずに高い白色度を有する電気亜鉛めっき鋼板を製造することが可能である。 In order to develop a method for producing an electrogalvanized steel sheet having high whiteness by the present inventors, as a result of repeated research, a total of one or more organic compounds having a mercapto group (-SH) is 0.5 to In the electrogalvanizing bath containing 30 mg / l, the electrolysis is divided into 5 or more times, and during each electrolysis, the steel plate is immersed in the acidic plating bath for 0.2 seconds or more, thereby increasing the whiteness. It has been found that an electrogalvanized steel sheet having a degree can be produced. Conventionally, the method of adding an organic compound to the plating bath generally has unavoidable adverse effects such as a glossy appearance, a decrease in current efficiency, or a shortened anode life, but in this method, whitening occurs at a very low addition concentration. Since an effect is obtained, it is possible to manufacture an electrogalvanized steel sheet having high whiteness without incurring the above-described adverse effects.
本発明は、このような知見に基づきなされたもので、その手段は以下のとおりである。 The present invention has been made on the basis of such findings, and the means thereof is as follows.
酸性めっき浴中で鋼板を陰極として電解して電気亜鉛めっき層を形成するに際し、メルカプト基(−SH)を有する有機化合物の1種又は2種以上を合計で0.5〜30mg/l含有する酸性めっき浴中で、電解を5回以上に分割して行うとともに、前記各々の電解の間に、鋼板を前記酸性めっき浴中に0.2秒以上浸漬する工程を有することを特徴とする電気亜鉛めっき鋼板の製造方法。 When forming an electrogalvanized layer by electrolysis using a steel plate as a cathode in an acidic plating bath, acidic plating containing one or more organic compounds having a mercapto group (-SH) in a total amount of 0.5 to 30 mg / l An electrogalvanized steel sheet characterized by having a step of immersing the steel sheet in the bath by dividing it into 5 or more times and immersing the steel sheet in the acid plating bath for 0.2 seconds or more between each electrolysis. Production method.
メルカプト基(−SH)を有する有機化合物は、めっきの最中にめっき(Zn)表面に吸着してZnの結晶成長を阻害し、また電析過電圧を上昇させ、2次核の発生を促進すると推定される(メルカプト基が、吸着に寄与していると考えられる)。そのために、Znめっき結晶の凹凸が微細化し、結果的に白色度が上昇するものと考えられる。 An organic compound having a mercapto group (—SH) is adsorbed on the surface of the plating (Zn) during the plating to inhibit the crystal growth of Zn, raises the electrodeposition overvoltage, and promotes the generation of secondary nuclei. Presumed (mercapto group is considered to contribute to adsorption). Therefore, it is considered that the unevenness of the Zn plating crystal becomes finer, and as a result, the whiteness increases.
本発明では、電解を5回以上に分割して行うとともに、前記各々の電解の間に、鋼板を前記酸性めっき浴中に0.2秒以上浸漬する工程を有する。これにより、初めて十分な白色度が得られるが、これは浸漬する工程において、メルカプト基(−SH)を有する有機化合物が鋼板表面に効果的に吸着する為と考えられる。 In the present invention, the electrolysis is performed by dividing it into 5 or more times, and a step of immersing the steel sheet in the acidic plating bath for 0.2 seconds or more between each electrolysis. Thus, sufficient whiteness can be obtained for the first time. This is considered to be because an organic compound having a mercapto group (-SH) is effectively adsorbed on the surface of the steel sheet in the dipping step.
本発明によれば、光沢度を大きく変化させずに、また、電流効率を大きく低下させずに、白色度の高い電気亜鉛めっき鋼板が得られる。また、電気亜鉛めっき処理後にクロメート又はクロメートフリーの各種化成処理(塗布型、反応型、電解型)や、更にその上に樹脂被覆処理等を実施した鋼板についても同様の効果は得られ、表面外観に優れた化成処理電気亜鉛めっき鋼板が得られることになる。 According to the present invention, an electrogalvanized steel sheet having high whiteness can be obtained without greatly changing the glossiness and without greatly reducing the current efficiency. The same effect can be obtained with steel sheets that have been subjected to various chemical treatments (coating type, reaction type, electrolytic type) that are chromate-free or chromate-free after electrogalvanizing treatment, and further resin coating treatment on the surface. Thus, a chemical conversion treated galvanized steel sheet excellent in the above can be obtained.
電気亜鉛めっき鋼板の製造においては通常、前処理として、鋼板表面を清浄化するための脱脂処理および水洗、さらに鋼板表面を活性化するための酸洗処理および水洗が施され、これらの前処理に引き続いて電気亜鉛めっきを実施する。 In the production of electrogalvanized steel sheets, as pretreatment, degreasing treatment and water washing for cleaning the steel plate surface and pickling treatment and water washing for activating the steel plate surface are generally performed. Subsequently, electrogalvanization is performed.
酸洗処理には、硫酸、塩酸、硝酸、及びこれらの混合物等各種の酸が使用できるが、硫酸、塩酸あるいはこれらの混合が望ましい。酸の濃度は特に規定しないが、酸化皮膜の除去能力、過酸洗による肌荒れ防止等を考慮すると、1〜20質量%程度が望ましい。酸洗処理液には、消泡剤、促進剤、抑制剤等を含有しても良い。抑制剤としては、鋼板(Fe)表面への吸着能の高いN系極性基を持つ水溶性有機化合物が代表例で、第一アミン(R1NH2)、第二アミン(R1R2NH)、第三アミン(R1R2R3N)あるいは第四アンモニウム塩(R1R2R3R4N+・X-)等が挙げられる。ここで、R1、R2、R3、R4は同一あるいは異なる炭化水素基を示し、X-はCl-等のアニオンを示す。 Various acids such as sulfuric acid, hydrochloric acid, nitric acid, and mixtures thereof can be used for the pickling treatment, but sulfuric acid, hydrochloric acid, or a mixture thereof is desirable. The concentration of the acid is not particularly specified, but is preferably about 1 to 20% by mass in consideration of the ability to remove the oxide film, prevention of rough skin by peracid washing, and the like. The pickling treatment liquid may contain an antifoaming agent, an accelerator, an inhibitor, and the like. Typical examples of inhibitors include water-soluble organic compounds with N-type polar groups that have a high adsorption capacity on the steel sheet (Fe) surface. Primary amines (R 1 NH 2 ), secondary amines (R 1 R 2 NH ), Tertiary amine (R 1 R 2 R 3 N) or quaternary ammonium salt (R 1 R 2 R 3 R 4 N + · X − ). Here, R 1 , R 2 , R 3 and R 4 represent the same or different hydrocarbon groups, and X − represents an anion such as Cl − .
本発明における電気亜鉛めっき工程では、メルカプト基(−SH)を有する有機化合物の1種又は2種以上を合計で0.5〜30mg/l含有する電気亜鉛めっき浴中で、電解を5回以上に分割して行うとともに、前記各々の電解の間に、鋼板を前記酸性めっき浴中に0.2秒以上浸漬する工程を有する。 In the electrogalvanizing step in the present invention, electrolysis is divided into 5 or more times in an electrogalvanizing bath containing 0.5 to 30 mg / l of one or more organic compounds having a mercapto group (-SH). And performing a step of immersing the steel plate in the acidic plating bath for 0.2 seconds or more between each electrolysis.
本発明で使用するメルカプト基(−SH)を有する有機化合物は、亜鉛への吸着能が特に高く、めっき結晶の凹凸を微細化させる効果が非常に大きいと考えられる。メルカプト基(−SH)を有する有機化合物としては、チオグリコール酸、メルカプトプロピオン酸、メルカプトコハク酸、3-メルカプト-1-プロパンスルホン酸ナトリウム、2-メルカプトエタノール、プロピルメルカプタン、エタンジチオールを例示できる。 The organic compound having a mercapto group (—SH) used in the present invention has a particularly high ability to adsorb to zinc, and it is considered that the effect of refining the unevenness of the plated crystal is very large. Examples of the organic compound having a mercapto group (—SH) include thioglycolic acid, mercaptopropionic acid, mercaptosuccinic acid, sodium 3-mercapto-1-propanesulfonate, 2-mercaptoethanol, propyl mercaptan, and ethanedithiol.
電気亜鉛めっき浴中のメルカプト基(−SH)を有する有機化合物の濃度が0.5mg/l未満では、白色度の上昇効果が不十分となり、濃度が0.5mg/l以上でめっきの白色化効果が得られる。濃度が30mg/lを超えるとめっき後外観の光沢化,薬品コストの上昇及び不溶性アノードの寿命短縮等の弊害が顕著となる。そのため、電気亜鉛めっき浴中に添加するメルカプト基(−SH)を有する有機化合物の濃度は0.5〜30mg/lとする。濃度が8mg/lを超えるとZnめっき電流効率が低下し、一定のZn付着量を得るのに必要な電気量が増加して製造コストが上昇する。そのため、0.5mg/l〜8mg/lがより好ましい濃度範囲である。前記濃度範囲では、光沢度が大きく変化することもない。 When the concentration of the organic compound having a mercapto group (—SH) in the electrogalvanizing bath is less than 0.5 mg / l, the whiteness increase effect is insufficient, and when the concentration is 0.5 mg / l or more, the whitening effect of plating is obtained. can get. When the concentration exceeds 30 mg / l, adverse effects such as glossy appearance after plating, increased chemical costs, and shortened life of insoluble anodes become significant. Therefore, the density | concentration of the organic compound which has a mercapto group (-SH) added to an electrogalvanization bath shall be 0.5-30 mg / l. When the concentration exceeds 8 mg / l, the Zn plating current efficiency decreases, and the amount of electricity necessary to obtain a constant amount of Zn deposition increases, resulting in an increase in manufacturing cost. Therefore, 0.5 mg / l to 8 mg / l is a more preferable concentration range. In the density range, the gloss does not change greatly.
本発明では、電気亜鉛めっき層を形成するに際し、電解を5回以上に分割して行い、各々の電解の間に、鋼板を0.2秒以上浸漬する工程を有する。鋼板をめっき浴中に浸漬する工程では、亜鉛めっき表面にメルカプト基(−SH)を有する有機化合物が効果的に吸着しているものと考えられる。 In the present invention, when forming the electrogalvanized layer, the electrolysis is performed by dividing it into 5 or more times, and the steel plate is immersed for 0.2 seconds or more between each electrolysis. In the step of immersing the steel sheet in the plating bath, it is considered that the organic compound having a mercapto group (—SH) is effectively adsorbed on the surface of the galvanizing.
この時間が0.2秒未満では、白色化効果が不十分となる。上限については特に規定しないが、時間が長くなるとめっき層の溶解量が増加し、必要なZn付着量を得る為の電解電気量が大きくなってしまう為、2秒以下が望ましい。また、電解を4回以下(浸漬の回数を3回以下)とすると、白色化効果が不十分となる。回数の上限については特に規定しないが、設備コストの上昇を防ぐためには、50回までが現実的である。 If this time is less than 0.2 seconds, the whitening effect is insufficient. The upper limit is not particularly specified, but as the time increases, the amount of dissolution of the plating layer increases, and the amount of electrolysis for obtaining the necessary Zn deposition amount increases. Moreover, when electrolysis is made 4 times or less (the number of immersions is 3 times or less), the whitening effect becomes insufficient. The upper limit of the number of times is not stipulated, but up to 50 times is realistic to prevent an increase in equipment costs.
めっき浴中のメルカプト基(−SH)を有する有機化合物の濃度を前記範囲に限定し、更に電解を5回以上に分割して行うとともに、前記各々の電解の間に、鋼板を前記酸性めっき浴中に0.2秒以上浸漬する工程を有することを除き、電気亜鉛めっきの浴条件及び電解条件については、特に限定されない。例えば、めっき浴としては硫酸浴、塩酸浴あるいは両者の混合などが適用できる。浴中にはZnイオンの他、添加剤あるいは不純物として硫酸ナトリウム、硫酸カリウム等の伝導度補助剤、Fe、Ni、Pb、Sn、Co等の金属イオン等を含有しても良い。浴条件についても特に限定しないが、例えば浴温を30〜70℃、pHを0.5〜4.5、相対流速を0〜4.0m/secとすれば良い。電解電流密度についても特に限定しないが、例えば10〜150A/dm2とすれば良い。電気亜鉛めっきの付着量についても特に限定しないが、通常5〜40g/m2程度である。 The concentration of the organic compound having a mercapto group (—SH) in the plating bath is limited to the above range, and the electrolysis is further divided into five or more times. There are no particular limitations on the electrogalvanizing bath conditions and electrolysis conditions except that it has a step of immersing in it for 0.2 seconds or longer. For example, a sulfuric acid bath, a hydrochloric acid bath, or a mixture of both can be applied as the plating bath. In addition to Zn ions, the bath may contain additives or impurities as conductivity aids such as sodium sulfate and potassium sulfate, metal ions such as Fe, Ni, Pb, Sn, and Co. The bath conditions are not particularly limited, but for example, the bath temperature may be 30 to 70 ° C., the pH may be 0.5 to 4.5, and the relative flow rate may be 0 to 4.0 m / sec. The electrolytic current density is not particularly limited, but may be, for example, 10 to 150 A / dm 2 . Not limited particularly also the adhesion amount of electro-galvanized, it is usually 5 to 40 g / m 2 approximately.
電気亜鉛めっき工程に引き続き、クロメート又はクロメートフリーの各種化成処理皮膜(塗布型、反応型、電解型)、更にその上に樹脂被覆処理等を実施した鋼板についても、本発明の効果は得られる。これらの処理を施した化成処理鋼板の外観は、無塗装で使用される場合電気亜鉛めっき後(化成処理前)の外観に大きく左右される(ただし1g/m2以上のりん酸亜鉛処理をする場合は外観が大きく変化するので除く)。そのために、本発明の方法により製造した電気亜鉛めっき鋼板を使用することにより、高い白色度を有する化成処理鋼板の製造が可能となるのである。 The effect of the present invention can also be obtained for steel sheets that have been subjected to various chemical conversion treatment films (coating type, reaction type, electrolytic type) that are chromate-free or chromate-free and further subjected to resin coating treatment on the chromate or chromate-free coating process. The appearance of the chemical conversion treated steel sheet after these treatments is greatly affected by the appearance after electrogalvanizing (before chemical conversion treatment) when used without coating (however, zinc phosphate treatment of 1 g / m 2 or more is applied) (Except because the appearance changes greatly). Therefore, the chemical conversion treatment steel plate which has high whiteness can be manufactured by using the electrogalvanized steel plate manufactured by the method of the present invention.
めっき原板として、厚さ0.7mmの冷延鋼板を使用した。これをアルカリで脱脂し、水洗した後、表1及び表2に示す条件で酸洗処理を実施した。酸洗液の温度は25℃である。なお、酸洗液には、一部で添加剤を使用したが、大部分は添加せずに酸洗を実施した。 A cold rolled steel sheet having a thickness of 0.7 mm was used as a plating original sheet. This was degreased with alkali, washed with water, and then pickled under the conditions shown in Tables 1 and 2. The temperature of the pickling solution is 25 ° C. Although some additives were used in the pickling solution, pickling was performed without adding most of the additives.
引き続き水洗した後、以下の条件で電気亜鉛めっきを実施した。なお、めっき浴には各種水溶性有機化合物を添加したが、一部のものについては添加せずにめっきを実施した。添加した添加剤の種類、濃度を表1及び表2に記載した。
・めっき浴:Zn2+イオン1.5mol/l含有する硫酸酸性浴、pH2.0、温度50℃
・相対流速:1.5m/sec
・電流密度:20〜120A/dm2
・電気量:600C/dm2
電気亜鉛めっきの際、電解途中で複数回、電解電流をカットし、鋼板を酸性めっき浴中に浸漬状態とした。なお、一部の鋼板については、電解電流をカットしなかった。
After subsequent water washing, electrogalvanization was performed under the following conditions. In addition, although various water-soluble organic compounds were added to the plating bath, plating was performed without adding some of them. The types and concentrations of the added additives are shown in Tables 1 and 2.
・ Plating bath: Acidic sulfuric acid bath containing 1.5 mol / l Zn 2+ ions, pH 2.0, temperature 50 ° C
・ Relative flow velocity: 1.5m / sec
・ Current density: 20 ~ 120A / dm 2
・ Electricity: 600C / dm 2
During electrogalvanization, the electrolysis current was cut several times during electrolysis, and the steel sheet was immersed in an acid plating bath. In addition, about some steel plates, the electrolysis current was not cut.
以上の条件で作製した電気亜鉛めっき鋼板について、白色度を明度(L値)で評価した。明度(L値)は、日本電色工業株式会社の色差計(SQ2000)を使用し、正反射を除いた条件(n-d)で測定した(JIS Z 8722 準拠)。
明度の測定結果は、以下の様に評価した。
◎:84≦L値
○:82≦L値<84
△:80≦L値<82
×:78≦L値<80
また、上記電気亜鉛めっき鋼板について、亜鉛めっき層を希塩酸で溶解し、原子吸光法でZn濃度を定量することによりめっき付着量(g/m2)を求め、電流効率を算出した。
About the electrogalvanized steel sheet produced on the above conditions, the whiteness was evaluated by the brightness (L value). The brightness (L value) was measured using a color difference meter (SQ2000) manufactured by Nippon Denshoku Industries Co., Ltd. under conditions (nd) excluding regular reflection (conforms to JIS Z 8722).
The brightness measurement results were evaluated as follows.
◎: 84 ≦ L value ○: 82 ≦ L value <84
Δ: 80 ≦ L value <82
×: 78 ≦ L value <80
Moreover, about the said electrogalvanized steel plate, the zinc plating layer was melt | dissolved with dilute hydrochloric acid, and the zinc adhesion amount (g / m < 2 >) was calculated | required by quantifying Zn density | concentration by an atomic absorption method, and the current efficiency was computed.
明度の評価結果、電流効率を表1及び表2に記載した。 The brightness evaluation results and the current efficiency are shown in Tables 1 and 2.
・発明例1〜23:L値向上効果が高い(L値62以上、評価○〜◎)。
・比較例1、3:電気亜鉛めっき浴中に添加するメルカプト基(−SH)を有する有機化合物の濃度が0.5mg/l未満であり、L値上昇効果が不十分。
・比較例2:電気亜鉛めっき浴中に添加するメルカプト基(−SH)を有する有機化合物の濃度が30mg/l超であり、L値向上効果はあるが、外観の光沢化が顕著であり、薬品コスト・アノード寿命の観点からも望ましくない。
・比較例4〜9:電気亜鉛めっき浴中に添加する有機化合物がメルカプト基(−SH)を有していない。L値上昇効果が認められない。
・比較例10、11:電解を複数回に分割せず、連続的に通電する例であり、L値上昇効果が不十分。
・比較例12、13:電解を分割してはいるものの、その回数が5回未満。L値上昇効果が不十分。
・比較例14、15:電解を分割してはいるものの、各々の電解の間での浸漬時間が0.2秒未満。L値上昇効果が不十分。
・比較例16、17:電気亜鉛めっき浴に水溶性有機化合物を添加しない例であり、L値上昇効果なし。
Invention Examples 1 to 23: L value improvement effect is high (L value of 62 or more, evaluation ○ to ◎).
Comparative Examples 1 and 3: The concentration of the organic compound having a mercapto group (-SH) added to the electrogalvanizing bath is less than 0.5 mg / l, and the L value increasing effect is insufficient.
Comparative Example 2: The concentration of the organic compound having a mercapto group (-SH) added to the electrogalvanizing bath is more than 30 mg / l, and there is an L value improving effect, but the glossiness of the appearance is remarkable, It is not desirable from the viewpoint of chemical cost and anode life.
Comparative Examples 4 to 9: The organic compound added to the electrogalvanizing bath does not have a mercapto group (—SH). L value increase effect is not recognized.
Comparative Examples 10 and 11: In this example, the electrolysis is not divided into a plurality of times and is continuously energized, and the effect of increasing the L value is insufficient.
Comparative Examples 12 and 13: Although the electrolysis is divided, the number of times is less than 5. L value increase effect is insufficient.
Comparative Examples 14 and 15: Although the electrolysis is divided, the immersion time between each electrolysis is less than 0.2 seconds. L value increase effect is insufficient.
Comparative Examples 16 and 17: In this example, no water-soluble organic compound is added to the electrogalvanizing bath, and there is no L value increasing effect.
本発明の電気亜鉛めっき鋼板は白色度が高く表面外観に優れる。そのため、特に家庭電化製品など、無塗装用途での使用に適している。 The electrogalvanized steel sheet of the present invention has high whiteness and excellent surface appearance. Therefore, it is particularly suitable for use in non-painting applications such as home appliances.
Claims (1)
When forming an electrogalvanized layer by electrolysis using a steel plate as a cathode in an acidic plating bath, acidic plating containing one or more organic compounds having a mercapto group (-SH) in a total amount of 0.5 to 30 mg / l An electrogalvanized steel sheet characterized by having a step of immersing the steel sheet in the bath by dividing it into 5 or more times and immersing the steel sheet in the acid plating bath for 0.2 seconds or more between each electrolysis. Production method.
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