KR20000041024A - Method for producing electrically zinc-plated steel sheet of excellent surface appearance - Google Patents

Method for producing electrically zinc-plated steel sheet of excellent surface appearance Download PDF

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KR20000041024A
KR20000041024A KR1019980056791A KR19980056791A KR20000041024A KR 20000041024 A KR20000041024 A KR 20000041024A KR 1019980056791 A KR1019980056791 A KR 1019980056791A KR 19980056791 A KR19980056791 A KR 19980056791A KR 20000041024 A KR20000041024 A KR 20000041024A
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steel sheet
zinc
plating
iron
bath
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KR1019980056791A
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KR100397296B1 (en
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곽영진
조용균
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이구택
포항종합제철 주식회사
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/22Electroplating: Baths therefor from solutions of zinc
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D7/00Electroplating characterised by the article coated
    • C25D7/06Wires; Strips; Foils
    • C25D7/0614Strips or foils
    • C25D7/0621In horizontal cells

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating Methods And Accessories (AREA)
  • Electroplating And Plating Baths Therefor (AREA)

Abstract

PURPOSE: A method is provided to produce electrically zinc-plated steel sheet of excellent surface appearance by restraining elution of iron from steel sheet due to low pH and by preventing charge of iron in a plated layer when plating with zinc electrically. CONSTITUTION: A zinc-plated steel sheet is produced by using a horizontal electrical plating facility using insoluble anode of bath in sulfate of zinc. Sodium iodide and potassium iodide of 0.0003mol/l-1mol/l is added to the plating bath to restrain melting of iron ions from the steel sheet. The difference of whiteness due to partial charge of iron occurring in phosphate treatment is restrained. Thereby, electrically zinc-plated steel sheet of excellent surface appearance is obtained.

Description

표면 외관이 우수한 전기아연 도금강판 제조방법Manufacturing method of galvanized steel sheet with excellent surface appearance

본 발명은 황산아연욕에서 전기 도금강판의 인산염 처리후 백색도의 차이로 인해 발생하는 흑색무늬 발생을 억제하여 표면외관이 우수한 전기 아연도금강판의 제조방법에 관한 것으로, 보다 상세하게는 수평형 전기도금조(LCC-H(Liquid Cushion Cell-Horizontal))에서 사용하고 있는 불용성 양극의 황산아연 도금욕에서 도금욕의 강산(pH 1.0∼1.4)에 의한 철의 용출을 억제하여 도금된 강판에 철과 아연의 공석으로 인한 인산염 처리 후 발생하는 흑색무늬를 방지하고자 도금욕에 요드화나트륨과 요드화칼륨을 첨가하여 황산아연욕에서 불순물로 존재하는 철의 농도를 전기 아연 도금후 인산염 처리후 백색도의 차이로 인해 발생되는 흑색무늬가 발생되지 않는 범위까지 줄이는 것을 특징으로 하는 황산아연욕에서 표면 외관이 우수한 전기 아연도금강판의 제조방법에 관한 것이다.The present invention relates to a method for producing an electrogalvanized steel sheet having excellent surface appearance by suppressing the occurrence of black pattern caused by the difference in whiteness after phosphate treatment of an electroplated steel sheet in a zinc sulfate bath, and more particularly, horizontal electroplating. In the zinc sulfate bath of the insoluble anode used in the tank (LCC-H (Liquid Cushion Cell-Horizontal)), iron and zinc were coated on the plated steel plate by suppressing the elution of iron by the strong acid (pH 1.0 to 1.4) of the plating bath. In order to prevent black pattern caused by phosphate treatment due to vacancies, sodium iron and potassium iodide were added to the plating bath, and the concentration of iron present as an impurity in the zinc sulfate bath was changed by the difference in whiteness after phosphate treatment after electrogalvanization. Manufacturing method of electrogalvanized steel sheet with excellent surface appearance in zinc sulfate bath, characterized in that it is reduced to the range where black pattern is not generated Relate to.

일반적으로 수평셀을 이용한 황산욕 도금은 기존 레디얼(radial)형의 염산욕 도금욕과 여러 가지 다른 면을 가지고 있는데, 기존의 염산욕과 달리 아연이온이 양극의 용해에 의해서 공급되지 않고 금속아연볼을 도금액에 용해시켜 공급하므로 도금액의 작업 pH를 1∼1.4 범위에서 낮게 관리하여 강판에 석출되는 아연양 만큼 아연이온을 신속히 보충할 수 있도록 되어있다. 따라서 낮은 도금액 pH로 인해 강판으로부터 용출된 철이온이 전기아연 도금시 도금층에 공석하게 되는데, 이 때 강판 전폭에 걸친 국부적 유속차이로 인해 도금과 전압 차이가 불균일하게 되어 전기아연 도금시 도금층에 공석되는 양이 다르게 된다. 이 때 이러한 공석양의 차이는 전기 아연도금만 했을 때는 도금층 표면외관 차이로 잘 나타나지 않으나, 인산염 처리를 하게 되면 도금층 철의 함량 차이에 의해 인산염피막의 색상차이로 인해 흑색무늬 윤곽이 더욱 뚜렷하게 나타나 표면외관을 해치게 된다. 이러한 문제를 해결하기 위해 도금액에 있는 이온 중 철이온만 선택적으로 제거하기 위해 킬레이트 시약에 의한 철이온의 제거방법이 있지만 고비용과 저효율등으로 적용하고 있지 못하다는 문제점이 있다.In general, sulfuric acid bath plating using a horizontal cell has many different aspects from a conventional radial hydrochloric acid plating bath. Unlike conventional hydrochloric acid baths, zinc ions are not supplied by dissolution of the anode, and thus zinc zinc balls are used. Since it is dissolved in the plating solution and supplied, the working pH of the plating solution is controlled to be low in the range of 1 to 1.4 so that zinc ions can be replenished as quickly as the amount of zinc deposited on the steel sheet. Therefore, the iron ions eluted from the steel sheet due to the low plating solution pH are vacant in the plating layer during electro zinc plating, where the difference in plating and voltage becomes uneven due to the local flow rate difference over the entire width of the steel sheet, and thus the vacancy in the plating layer during electro zinc plating. The amount is different. At this time, the difference in the amount of vacancies is not shown as a difference in the surface appearance of the plating layer only by electro galvanization, but when the phosphate treatment is performed, the black pattern contour is more clearly displayed due to the color difference of the phosphate coating due to the difference in the iron content of the plating layer. It hurts the appearance. In order to solve this problem, there is a method of removing iron ions by chelating reagent to selectively remove only iron ions among ions in the plating solution, but there is a problem in that it is not applied due to high cost and low efficiency.

본 발명은 상기와 같은 문제점을 해결하기 위하여 안출된 것으로서, 수평셀을 이용한 불용성 양극을 사용하는 황산욕에서, 낮은 pH로 인하여 강판으로부터 철이 용출되는 것을 억제하여 전기 아연 도금시 철이 도금층에 공석되는 것을 방지하여 인산염 처리후 표면외관이 우수한 전기 아연도금강판을 제조하는 방법을 제공하는 것을 그 목적으로 한다.The present invention has been made to solve the above problems, in the sulfuric acid bath using an insoluble anode using a horizontal cell, it is suppressed that iron is eluted from the steel sheet due to the low pH to prevent the iron vacancy in the plating layer during electro-galvanization It is an object of the present invention to provide a method for producing an electrogalvanized steel sheet having excellent surface appearance after phosphate treatment.

본 발명은 상기 목적을 달성하기 위하여, 황산아연욕의 불용성 양극을 사용하는 수평형 전기도금 설비를 이용한 아연도금강판의 제조방법에서, 상기 도금욕에 요드화나트륨과 요드화칼륨을 0.0003mol/l 이상 1mol/l 미만으로 첨가하므로서 강판으로부터 철이온의 용해를 억제하여 도금후 인산염 처리시 발생하는 철의 부분공석에 따른 백색도 차이를 억제할 수 있는 표면외관이 우수한 전기 아연도금강판 제조방법을 제공하는 것을 특징으로 한다.In order to achieve the above object, the present invention provides a method for producing a galvanized steel sheet using a horizontal electroplating apparatus using an insoluble anode of zinc sulfate bath, the sodium bath and potassium iodide 0.0003mol / l in the plating bath By providing less than 1 mol / l to suppress the dissolution of iron ions from the steel sheet to provide a method for producing an electrogalvanized steel sheet excellent in surface appearance that can suppress the difference in whiteness due to partial vacancy of iron generated during phosphate treatment after plating It is characterized by.

도 1은 황산아연 도금액중 요드화나트륨과 요드화칼륨의 첨가량에 따른 강판의 철의 용해 억제율을 나타내는 그래프도.BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a graph showing the iron dissolution inhibition rate of steel sheet according to the amount of sodium iodide and potassium iodide added in zinc sulfate plating solution.

이하, 본 발명에 대하여 보다 상세하게 설명한다.EMBODIMENT OF THE INVENTION Hereinafter, this invention is demonstrated in detail.

본 발명은 요드화나트륨과 요드화칼륨과 같은 무기 억제제를 이용하여 전기아연 도금의 황산욕에서 음극으로 이용되고 있는 강판에 화학흡착을 하여 강판의 부식을 억제하여 강판의 철이온의 용출을 억제하는 방법이다.The present invention uses an inorganic inhibitor such as sodium iodide and potassium iodide to chemically adsorb the steel sheet used as a cathode in the sulfuric acid bath of electro-zinc plating to inhibit the corrosion of the steel sheet to suppress the elution of iron ions of the steel sheet Way.

일반적으로 아연은 강판표면에 도금되어 방식작용을 함으로써 소지철을 보호하고, 도금이 용이하기 때문에 자동차용 강판재 혹은 가전용 강판재에 오래전부터 이용되어 왔다. 전기 아연도금조는 크게 수평형, 수직형, 레이디얼형으로 나눌 수 있으며, 도금액에 따라 염산욕과 황산욕으로 그리고 양극의 용해에 따라 가용성과 불용성 양극으로 나눌 수 있다. 이중에서 도금조직 및 표면외관이 우수하고 극간거리 감소로 고전류밀도 작업이 가능한 장점을 가지고 있는 불용성 양극을 적용하면서 황산욕을 기본으로 하는 설비는 금속 아연볼을 도금용액으로 용해시켜 아연이온을 공급해주는 방식을 채택하고 있다. 따라서 도금욕의 pH가 1.0-1.4의 범위에서 금속아연의 용해율을 증가시켜 아연이 강판에 석출되는 양 이상만큼 아연이온을 공급해 줄 수 있다.In general, zinc is plated on the surface of the steel plate to protect the base iron by anticorrosive action, and since the plating is easy, it has been used for a long time in automotive steel sheet or automotive steel sheet. The electroplating bath can be divided into horizontal, vertical, and radial type, and it can be divided into hydrochloric acid bath and sulfuric acid bath depending on the plating solution and soluble and insoluble anode depending on the dissolution of the anode. Among them, the insoluble anode, which has excellent plating structure and surface appearance, and has the advantage of high current density work by reducing the distance between poles, and the sulfuric acid bath-based equipment dissolves metal zinc balls with plating solution to supply zinc ions. The system is adopted. Therefore, by increasing the dissolution rate of the metal zinc in the pH of the plating bath 1.0-1.4 it can supply zinc ions more than the amount of zinc precipitated on the steel sheet.

하지만 도금액의 pH가 낮아 소지강판의 도금용액에 대한 용해속도가 증가하여 강판에서 철이온이 용출되어 용액중에 불순물로 존재하게 된다.However, since the pH of the plating solution is low, the dissolution rate of the plated steel sheet increases with the plating solution, and iron ions are eluted from the steel sheet, and thus they exist as impurities in the solution.

이와같은 철이온은 아연의 석출전위와 비교하여 볼 때 약 0.32V 정도 귀한 금속이기 때문에 석출이 용이하여 아연과 철이온이 존재하는 도금욕에서 아연과 동시에 강판상에 공석을 하게 된다.Such iron ions are about 0.32V precious metals compared to the precipitation potential of zinc, so they are easily precipitated and are vacant on the steel plate simultaneously with zinc in the plating bath in which zinc and iron ions are present.

이 때 강판의 국부적 도금과 전압 차이에 따라 강판에 공석되는 양이 다르게 되어, 이러한 공석양의 차이는 전기도금된 강판을 인산염 처리한 후 살펴 보면 심한 백색도 차이로 인하여 도금액 흐름 무늬 모양의 흑색무늬 결함이 나타나게 되는 것이다.At this time, the amount of vacancies in the steel sheet is different according to the local plating of the steel sheet and the voltage difference, and the difference in the amount of vacancies is caused by the plating pattern flow pattern black pattern defect due to the severe whiteness difference after phosphate treatment of the electroplated steel sheet. Will appear.

그러나 소지 강판은 높은 흡착에너지를 가지는 금속으로 높은 표면에너지를 가져서 전기도금 황산욕에 요드화나트륨 혹은 요드화칼륨을 소량 첨가하면 철의 표면에 철과 요오드가 화학적으로 표면 결합을 형성하여 강판 표면부터 Fe2+가 용액쪽으로 확산되어 가는 것을 막을 뿐만 아니라 H+이온이 도금용액부터 금속표면에의 접근을 막는 효과로 인하여 강판의 용해속도는 굉장히 느려진다. 이 조건에서 양이온은 칼륨과 나트륨은 강판에 흡착하지 않고 황산욕의 전도보조제의 역할로 이온들의 영동에 영향을 미치고 전극 프로세스의 속도에 영향을 미치지 않는다. 이 요드화나트륨과 요드화칼륨은 철에 대해서만 선택적으로 용해 억제 작용을 하여 금속 아연볼을 용해하는데 문제가 없다.However, the steel sheet is a metal with high adsorption energy and has high surface energy. When a small amount of sodium iodide or potassium iodide is added to the electroplating sulfuric acid bath, iron and iodine chemically form surface bonds on the surface of the steel sheet. In addition to preventing Fe 2+ from diffusing into the solution, the rate of dissolution of the steel sheet is very slow due to the effect of H + ions preventing access from the plating solution to the metal surface. Under these conditions, the cations do not adsorb potassium and sodium to the steel sheet, but act as a conduction aid in the sulfuric acid bath, which affects the phoresis of ions and does not affect the speed of the electrode process. This sodium iodide and potassium iodide selectively dissolve and inhibit the metal zinc ball so that there is no problem in dissolving the metal zinc ball.

이하, 실시예를 들어 본 발명을 보다 상세하게 설명한다.Hereinafter, an Example is given and this invention is demonstrated in detail.

(실시예)(Example)

본 발명의 실험과정은 먼저 강판이 도금액에 용출되는 속도를 측정하기 위하여 두께가 0.7mm인 시편을 33ψ로 균일하게 절단한 후 초음파로 3회 세척 및 탈지 건조하여, 표 1에 나타난 도금액 조성에 요드화나트륨과 요드화칼륨을 0.0001∼1M(mol/l)까지 첨가량을 변화시켜 유리 덮개가 있는 도금액 1L의 비이커에 놓고 30분간 침적한 후 시험 전과 후의 무게감량차를 이용하여 다음 (1)식에 의해 용해 억제율을 구하였다.In the experimental procedure of the present invention, in order to measure the rate at which the steel sheet elutes into the plating solution, the specimen having a thickness of 0.7 mm was uniformly cut into 33ψ, and then washed and degreased three times with ultrasonic waves. Change the amount of sodium sulfide and potassium iodide to 0.0001 ~ 1M (mol / l), place it in a beaker of 1L of plating solution with glass cover, and soak for 30 minutes, and then use the weight loss difference before and after the test. The inhibition of dissolution was determined by

용해억제율(%) = (1- W˚/W)x100 (1)Melt inhibition rate (%) = (1- W˚ / W) x100 (1)

여기서 W=요드화나트륨과 요드화칼륨이 들어있지 않는 용액에서의 시편 무게 감소량Where W = weight loss of the specimen in a solution free of sodium iodide and potassium iodide

W˚= 요드화나트륨과 요드화칼륨이 들어있는 용액에서의 시편 무게 감소량W˚ = specimen weight loss in solution containing sodium iodide and potassium iodide

또한 표 1의 용액 조성에 첨가량을 변화시키면서 표 2의 도금조건으로 대형도금조를 이용하여 120A/dm2으로 일정하게 도금하면서 도금의 외관 및 밀착성에 영향을 주는지를 알아보았다.In addition, while varying the addition amount in the solution composition of Table 1, it was examined whether the plating and coating properties of the table 2 in a constant plating at 120A / dm 2 using a large plating bath affects the appearance and adhesion of the plating.

도금에 사용한 음극시편의 크기는 100x200mm 이었고 도금부착량은 20g/m2으로 하였으며, 양극과 음극간의 극간거리는 10mm이었다.The size of the negative electrode specimen used for plating was 100x200mm, the coating weight was 20g / m 2 , and the gap distance between the positive electrode and the negative electrode was 10mm.

아연(g/l)Zinc (g / l) PHPH 온도(℃)Temperature (℃) 6060 1.21.2 6060

온도 (℃)Temperature (℃) PHPH 전류밀도(A/dm2)Current density (A / dm 2 ) 도금부착량(g/dm2)Coating Weight (g / dm 2 ) 유속(m/sec)Flow rate (m / sec) 6060 1.21.2 120120 2020 1.51.5

도 1은 기존의 도금액에 요드화 나트륨과 요드화 칼륨을 첨가하지 않은 경우와 첨가한 경우에 대한 용해 억제율을 보여주고 있다. 용액중에 요드화나트륨과 요드화칼륨이 0.1∼0.6M/l만 존재하여도 철의 용해 억제율이 기존 도금 용액의 대비하여 90% 이상에 달하는 것을 알 수 있다.FIG. 1 shows the dissolution inhibition rate for the case where the sodium iodide and potassium iodide were not added to the existing plating solution and when they were added. Even if only 0.1-0.6 M / l of sodium iodide and potassium iodide are present in the solution, it can be seen that the iron dissolution inhibition rate reaches 90% or more compared to the existing plating solution.

표 3은 도금용액에 요드화나트륨과 요드화칼륨의 첨가량에 따른 도금 후 표면외관 및 밀착성의 결과를 나타내주고 있다.Table 3 shows the results of surface appearance and adhesion after plating depending on the amount of sodium iodide and potassium iodide added to the plating solution.

구분division 첨가량(mol/l)Addition amount (mol / l) 백색도Whiteness 광택도Glossiness 밀착성Adhesion 흑색무늬발생Black pattern occurrence 비교예Comparative example 00 1One 1One 1One 발생Occur 0.00020.0002 1One 1One 1One 발생Occur 발명예Inventive Example 0.00030.0003 1One 1One 1One 미발생Not Occurred 0.0010.001 1One 1One 1One 미발생Not Occurred 0.10.1 1One 1One 1One 미발생Not Occurred 0.50.5 1One 1One 1One 미발생Not Occurred 1One 1One 1One 1One 미발생Not Occurred

* 평가정도: 좋음 ← 1∼6 → 나쁨* Rating: Good ← 1 ~ 6 → Poor

비교예에서 첨가량이 0.0002mol/l인 경우에는 도금 후 강판의 표면외관 및 밀착성에는 문제는 없지만 도 1에서 나타나듯이 용해 억제율이 현저히 낮아 철이온이 강판에서 용해되어 도금시 아연과 함께 공석될 가능성이 높아, 인산염 처리 후 약간의 흑색무늬 발생을 띄었다. 따라서 발명예에서 제시한 요드화나트륨과 요드화 칼륨을 0.0003∼1mol/l를 황산욕에 첨가하여 강판의 철의 용해도를 현저히 억제하여, 전기 아연도금시 도금욕의 불순물로 존재하는 철의 도금된 강판의 부분 공석을 억제하여 도금 후 인삼염 처리에서 발생할 수 있는 흑색무늬 발생을 억제할 수 있고, 동시에 도금 효율 및 도금 품질에는 전혀 영향을 미치지 않는 효과가 있다.In the comparative example, when the addition amount is 0.0002 mol / l, there is no problem in the surface appearance and adhesion of the steel sheet after plating, but as shown in FIG. 1, the dissolution inhibition rate is remarkably low, so that iron ions are dissolved in the steel sheet and may be vacated together with zinc during plating. High, showing slight black pattern after phosphate treatment. Thus, 0.0003 to 1 mol / l of sodium iodide and potassium iodide as described in the present invention was added to the sulfuric acid bath to significantly suppress the solubility of iron in the steel sheet, and plated iron present as an impurity of the plating bath during electroplating. By suppressing partial vacancy of the steel sheet, it is possible to suppress the generation of black patterns that may occur in the ginseng treatment after plating, and at the same time, there is no effect on plating efficiency and plating quality.

상술한바와 같이, 본 발명에 의하면, 황산아연욕의 불용성 양극을 사용하는 전기도금 설비에서 도금욕의 낮은 pH 조업조건에서 발생하는 강판의 철의 용해를 억제하고자, 도금욕에 요드화나트륨 및 요드화칼륨을 0.0003mol/l 이상, 1mol/l 이하 미만으로 첨가하여 철의 용해를 억제하여, 도금시 발생할 수 있는 도금강판의 철의 공석을 방지하여 인산염 처리 후 발생할 수 있는 흑색무늬 발생을 억제하여 표면외관이 우수한 전기 아연도금강판을 제조할 수 있다.As described above, according to the present invention, sodium iodide and iodine in the plating bath to suppress the iron dissolution of the steel sheet generated in the low pH operating conditions of the plating bath in the electroplating equipment using an insoluble anode of zinc sulfate bath. By suppressing iron dissolution by adding potassium sulfide to more than 0.0003mol / l and less than 1mol / l, it prevents the vacancy of iron in the plated steel sheet and prevents black pattern generation after phosphate treatment. An electrogalvanized steel sheet having excellent surface appearance can be produced.

Claims (1)

황산아연욕의 불용성 양극을 사용하는 수평형 전기도금 설비를 이용한 아연도금강판의 제조방법에서, 상기 도금욕에 요드화나트륨과 요드화칼륨을 0.0003mol/l 이상, 1mol/l 미만으로 첨가하므로서 강판으로부터 철이온의 용해를 억제하여 도금후 인산염 처리시 발생하는 철의 부분공석에 따른 백색도 차이를 억제할 수 있는 것을 특징으로 하는 표면외관이 우수한 전기 아연도금강판 제조방법.In the method for producing a galvanized steel sheet using a horizontal electroplating apparatus using an insoluble anode of zinc sulfate bath, the steel sheet is added to the plating bath by adding sodium iodide and potassium iodide at least 0.0003 mol / l and less than 1 mol / l. Method for producing an electro-galvanized steel sheet having excellent surface appearance, characterized by suppressing the dissolution of iron ions from the white ions due to partial vacancy of iron generated during phosphate treatment after plating.
KR10-1998-0056791A 1998-12-21 1998-12-21 Manufacturing method of electro galvanized steel sheet with excellent surface appearance KR100397296B1 (en)

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Cited By (2)

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Publication number Priority date Publication date Assignee Title
KR20040078878A (en) * 2003-03-06 2004-09-13 니찌아스 카부시키카이샤 Anti-squeal shim and structure for attaching the same
KR100916907B1 (en) * 2002-09-12 2009-09-09 주식회사 포스코 a method of manufacturing an electro-galvanized sheets with uniform surface appearance

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KR870002075B1 (en) * 1984-08-30 1987-12-03 한국과학기술원 Zinc electrolysis method of saving energy
KR100322034B1 (en) * 1997-09-27 2002-04-17 이구택 Plating solution suitable for the manufacture of electro galvanized steel sheet with excellent surface appearance
KR19990084931A (en) * 1998-05-12 1999-12-06 이구택 Manufacturing method of electro galvanized steel sheet with excellent black pattern resistance

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100916907B1 (en) * 2002-09-12 2009-09-09 주식회사 포스코 a method of manufacturing an electro-galvanized sheets with uniform surface appearance
KR20040078878A (en) * 2003-03-06 2004-09-13 니찌아스 카부시키카이샤 Anti-squeal shim and structure for attaching the same

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