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CN103952735B - A kind of continuous copper-plating of steel strip technique - Google Patents

A kind of continuous copper-plating of steel strip technique Download PDF

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CN103952735B
CN103952735B CN201410194964.4A CN201410194964A CN103952735B CN 103952735 B CN103952735 B CN 103952735B CN 201410194964 A CN201410194964 A CN 201410194964A CN 103952735 B CN103952735 B CN 103952735B
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plating
degreasing
steel strip
copper plating
electroplating
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CN103952735A (en
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郑伟
石磊
栾玉青
徐勇
刘科高
宋文婷
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Shandong Jianzhu University
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Abstract

A kind of continuous copper-plating of steel strip technique adopts cyanide copper plating process to electroplate.Mainly include pretreatment process and electro-coppering process.Pre-treatment mainly includes ultrasonic oil removal, electrolytic degreasing, washing, activation, washing;Electroplating process mainly includes copper facing, recovery, washing.Technology groove in continuous copper-plating of steel strip adopts the isosceles trapezoid groove with transparent openable observation window of closed, and cell body is designed as the cell body that top is isosceles trapezoid;Three transparent openable observation windows are respectively designed at the position, two slopes of groove;Article two, be respectively provided with between steel band and 3 anodes 4 block lengths equal there is nonmetal baffle plate corrosion-resistant, resistant to elevated temperatures, substantial amounts of electric lines of force, coating uniform ground will not be assembled in the edge of steel band.

Description

一种钢带连续镀铜工艺A continuous copper plating process for steel strip

技术领域technical field

本发明涉及碱性镀铜的技术领域,具体是一种钢带连续镀铜工艺。The invention relates to the technical field of alkaline copper plating, in particular to a continuous copper plating process for steel strips.

背景技术Background technique

随着我国工业的发展,尤其是汽车等行业的飞速发展,对铜及铜制品的需求量日益增加。但是我国是一个贫铜国家,铜主要依赖进口,加上国际上铜价格上升很快,给我国汽车等产业带来较大成本压力。经过论证和实践证明,在汽车,家电等行业,钢材镀铜制品代替铜制品是可行的,甚至在某些方面的性能反而比铜更好些。镀铜钢带主要用来生产帮迪管,普遍应用在汽车油管、地板加热管、空调管等方面。以铁代铜不但是经济问题,还能大量减少碳排放。所以说钢带镀铜具有良好的社会效益和经济效益。利用氰化镀铜,可以得到致密、平整、结合力良好的镀层,所以钢带连续镀铜采用氰化镀铜工艺。在钢带生产中,阳极与钢带之间的电力线容易在钢带边缘聚集,导致钢带镀层产生厚度的差异,影响镀层的性能。With the development of my country's industry, especially the rapid development of automobile and other industries, the demand for copper and copper products is increasing day by day. However, my country is a copper-poor country. Copper mainly depends on imports. In addition, the price of copper in the world has risen rapidly, which has brought great cost pressure to my country's automobile and other industries. After demonstration and practice, it is feasible to replace copper products with copper-plated steel products in industries such as automobiles and home appliances, and even have better performance than copper in some aspects. Copper-plated steel strips are mainly used to produce help pipes, which are widely used in automobile oil pipes, floor heating pipes, air-conditioning pipes, etc. Substituting iron for copper is not only an economic issue, it can also greatly reduce carbon emissions. Therefore, copper plating on steel strip has good social and economic benefits. Cyanide copper plating can be used to obtain a dense, smooth, and well-bonded coating, so the continuous copper plating of steel strips adopts the cyanide copper plating process. In the production of steel strip, the electric force lines between the anode and the steel strip tend to gather at the edge of the steel strip, resulting in differences in the thickness of the steel strip coating, which affects the performance of the coating.

发明内容Contents of the invention

一种钢带连续镀铜工艺,主要包括前处理过程和电镀铜过程。前处理主要包括化学除油、电解除油、水洗、活化、水洗;电镀过程主要包括预镀铜、主镀铜、回收、水洗。在钢带连续镀铜中的工艺槽采用密闭式的带有透明的可开启的观察窗的等腰梯形槽,槽体设计为上方是等腰梯形的槽体;在槽的两个斜坡部位各设计有三个透明的可开启的观察窗;两条钢带与3个阳极之间各设有4块长度相等的具有耐腐蚀、耐高温的非金属挡板;在钢带生产中,高电流区往往在钢带边缘处,即边缘效应,边缘效应会导致高电流区和低电流区镀层的厚度差异较大,加上具有耐腐蚀性、耐高温的非金属挡板后,钢带与阳极之间的电力线可以绕过挡板,钢带的边缘不会聚集大量的电力线,镀层均匀平整。A continuous copper plating process for a steel strip mainly includes a pretreatment process and an electroplating copper process. Pretreatment mainly includes chemical degreasing, electrolytic degreasing, water washing, activation, and water washing; electroplating process mainly includes pre-copper plating, main copper plating, recycling, and water washing. The process tank in the continuous copper plating of steel strip adopts a closed isosceles trapezoidal tank with a transparent and openable observation window, and the tank body is designed as an isosceles trapezoidal tank body above; It is designed with three transparent observation windows that can be opened; between the two steel strips and the three anodes, there are four non-metallic baffles of equal length with corrosion resistance and high temperature resistance; in the production of steel strips, the high current area It is often at the edge of the steel strip, that is, the edge effect. The edge effect will cause a large difference in the thickness of the coating in the high-current area and the low-current area. After adding a non-metallic baffle with corrosion resistance and high temperature resistance, the gap between the steel strip and the anode The power lines between them can go around the baffle, and the edge of the steel belt will not gather a large number of power lines, and the coating is even and flat.

具体实施方式detailed description

本发明提供的一种钢带连续镀铜工艺,主要包括前处理过程和电镀铜过程,前处理主要包括化学除油、电解除油、水洗、活化、水洗;电镀过程主要包括镀铜、回收、水洗。其中除油处理采用超声波除油与阴-阳极联合除油相互结合的方式。A continuous copper plating process for a steel strip provided by the present invention mainly includes a pretreatment process and an electroplating copper process. The pretreatment mainly includes chemical degreasing, electrolytic degreasing, water washing, activation, and water washing; the electroplating process mainly includes copper plating, recycling, wash. Among them, the degreasing treatment adopts the combination of ultrasonic degreasing and cathode-anode joint degreasing.

1.热水洗采用70~80℃的热水清洗20~30s。1. Hot water washing Use hot water at 70-80°C for 20-30 seconds.

2.除油处理包括超声波除油与电解除油,电解除油为阴-阳极联合除油。首先,进行化学除油,时间为1~3min,然后进行电解除油,电解除油时,首先阴极除油1min,然后阳极除油15s。2. Degreasing treatment includes ultrasonic degreasing and electrolytic degreasing, and electrolytic degreasing is cathode-anode joint degreasing. First, chemical degreasing is carried out for 1-3 minutes, and then electrolytic degreasing is carried out. When electrolytic degreasing is performed, the cathodic degreasing is first performed for 1 min, and then the anode is degreased for 15 s.

所述的超声波除油,超声波除油清洗剂,浓度为5%,温度为40~50°C,超声波频率为25kHz。Described ultrasonic degreasing, ultrasonic degreasing cleaning agent, concentration is 5%, temperature is 40~50 ℃, and ultrasonic frequency is 25kHz.

3.活化处理中,活化液中的侵蚀剂为盐酸,浓度20g/L,溶液温度为35±5℃,阴极电流密度为7~10A/dm2,侵蚀时间为20~30s。3. In the activation treatment, the etching agent in the activation solution is hydrochloric acid, the concentration is 20g/L, the solution temperature is 35±5°C, the cathode current density is 7-10A/dm 2 , and the etching time is 20-30s.

4.除油后的水洗和活化后的水洗均采用浓度为0.5μS以下的纯水,进行清洗,清洗水温为30~40℃。4. The water washing after degreasing and the water washing after activation all use pure water with a concentration of 0.5μS or less for cleaning, and the temperature of the washing water is 30-40°C.

5.一种钢带连续镀铜工艺,其中电镀过程是连续镀铜过程。镀铜的镀液主要由氰化亚铜、氰化钠和氢氧化钠组成,电镀时阴极电流密度为0.2~2A/dm2,温度为55~65℃,镀层的厚度由电流和卷带机带速控制。各过程中的清洗水洗采用浓度为0.5μS以下的纯水。5. A continuous copper plating process for a steel strip, wherein the electroplating process is a continuous copper plating process. The copper plating solution is mainly composed of cuprous cyanide, sodium cyanide and sodium hydroxide. During electroplating, the cathode current density is 0.2-2A/dm2, and the temperature is 55-65°C. The thickness of the coating is determined by the current and the tape winding machine. speed control. Cleaning water in each process uses pure water with a concentration of 0.5 μS or less.

实施例1Example 1

在钢带连续镀铜中的工艺槽采用密闭式的带有透明的自动开启的观察窗的等腰梯形槽,槽体设计为上方是等腰梯形的槽体;在槽的两个斜坡部位各设计有三个透明的可开启的观察窗;两条钢带与3个阳极之间各设有4块长度相等的具有耐腐蚀、耐高温的非金属挡板;在钢带生产中,高电流区往往在钢带边缘处,即边缘效应,边缘效应会导致高电流区和低电流区镀层的厚度差异较大,加上具有耐腐蚀性、耐高温的非金属挡板后,钢带与阳极之间的电力线可以绕过挡板,钢带的边缘不会聚集大量的电力线,镀层均匀平整。The process tank in the continuous copper plating of the steel strip adopts a closed isosceles trapezoidal tank with a transparent automatic opening observation window, and the tank body is designed as an isosceles trapezoidal tank body above; It is designed with three transparent observation windows that can be opened; between the two steel strips and the three anodes, there are four non-metallic baffles of equal length with corrosion resistance and high temperature resistance; in the production of steel strips, the high current area It is often at the edge of the steel strip, that is, the edge effect. The edge effect will cause a large difference in the thickness of the coating in the high-current area and the low-current area. After adding a non-metallic baffle with corrosion resistance and high temperature resistance, the gap between the steel strip and the anode The power lines between them can go around the baffle, and the edge of the steel belt will not gather a large number of power lines, and the coating is even and flat.

Claims (1)

1.一种钢带连续镀铜工艺,采用氰化镀铜工艺进行电镀,主要包括前处理过程和电镀铜过程,前处理主要包括超声波除油、电解除油、水洗、活化、水洗;电镀过程主要包括镀铜、回收、水洗,其特征在于:在钢带连续镀铜中的工艺槽采用密闭式的带有透明的可开启的观察窗的等腰梯形槽,槽体设计为上方是等腰梯形的槽体;在槽的两个斜坡部位各设计有三个透明的可开启的观察窗;两条钢带与3个阳极之间各设有4块长度相等的具有耐腐蚀、耐高温的非金属挡板;1. A continuous copper plating process for steel strips, which adopts the cyanide copper plating process for electroplating, mainly includes a pretreatment process and an electroplating copper process, and the pretreatment mainly includes ultrasonic degreasing, electrolytic degreasing, washing, activation, and washing; the electroplating process It mainly includes copper plating, recycling, and water washing. It is characterized in that: the process tank in the continuous copper plating of steel strips adopts a closed isosceles trapezoidal tank with a transparent and openable observation window, and the tank body is designed to be isosceles Trapezoidal trough body; three transparent and openable observation windows are designed on the two slopes of the trough; four equal-length non-corrosion and high temperature resistant metal baffle; (1)前处理过程中的超声波除油,超声波除油清洗剂,浓度为5%,温度为40~50℃,超声波频率为25kHz;(1) Ultrasonic degreasing in the pretreatment process, ultrasonic degreasing cleaning agent, the concentration is 5%, the temperature is 40~50°C, and the ultrasonic frequency is 25kHz; (2)前处理过程中电解除油液为活性碱,碱液温度为60~80℃,电流密度为8~10A/dm2(2) During the pretreatment process, the electrolytic deoiling solution is active alkali, the temperature of the alkali solution is 60-80°C, and the current density is 8-10A/dm 2 ; (3)前处理过程中电解除油采用阴-阳极联合除油,其中阴极除油时间长,阳极除油时间短;(3) In the pretreatment process, electrolytic degreasing adopts cathode-anode joint degreasing, in which the cathode degreasing time is long, and the anode degreasing time is short; (4)前处理过程中活化液中的侵蚀剂为盐酸,浓度20g/L,溶液温度为35±5℃,阴极电流密度为7~10A/dm2,侵蚀时间为20~30s;(4) The etching agent in the activation solution in the pretreatment process is hydrochloric acid, the concentration is 20g/L, the solution temperature is 35±5°C, the cathode current density is 7-10A/dm 2 , and the erosion time is 20-30s; (5)电镀铜中采用依次排列的6个镀槽,1个回收槽和1个清洗槽;(5) 6 plating tanks, 1 recovery tank and 1 cleaning tank arranged in sequence are used in copper electroplating; (6)在钢带连续镀铜中镀槽内镀液通过过滤机的循环过滤,加速电沉积速度;(6) In the continuous copper plating of the steel strip, the plating solution in the plating tank passes through the circulating filtration of the filter to accelerate the electrodeposition speed; (7)在钢带连续镀铜中电镀槽的钢带出口处采用雾化喷淋的方式对钢带上的镀液进行回收;(7) adopt the mode of atomization spray to reclaim the plating solution on the steel strip at the steel strip outlet of the electroplating bath in the continuous copper plating of the steel strip; (8)镀铜采用多工位连续电镀的方式,镀液主要由氰化亚铜、氰化钠和氢氧化钠组成,电镀时阴极电流密度为0.2~2A/dm2,温度为55~65℃,镀铜层的厚度根据电流或传送速度决定;(8) Copper plating adopts the method of multi-station continuous electroplating. The plating solution is mainly composed of cuprous cyanide, sodium cyanide and sodium hydroxide. During electroplating, the cathode current density is 0.2-2A/dm 2 and the temperature is 55-65 ℃, the thickness of the copper plating layer is determined by the current or transmission speed; (9)各过程中的清洗水洗采用电导率为0.5μS以下的纯水。(9) Cleaning and washing in each process uses pure water with a conductivity of 0.5 μS or less.
CN201410194964.4A 2014-05-11 2014-05-11 A kind of continuous copper-plating of steel strip technique Expired - Fee Related CN103952735B (en)

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CN107604399A (en) * 2017-10-31 2018-01-19 广东骏亚电子科技股份有限公司 A kind of electro-plating method based on ultrasonic wave
CN110666279A (en) * 2019-10-15 2020-01-10 国营第六一六厂 Brazing method for aluminum bronze pipe joint
CN114214682B (en) * 2021-12-22 2023-05-30 东莞市金瑞五金股份有限公司 Electroplating process and electroplating equipment for copper plating of workpiece

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4050996A (en) * 1976-11-03 1977-09-27 General Motors Corporation Electochemically exchanging a steel surface with a pure iron surface
US4582573A (en) * 1985-02-25 1986-04-15 Comet Research, Inc. Method for treating a single side of a metallic sheet
CN101665962A (en) * 2009-09-04 2010-03-10 厦门大学 Alkaline non-cyanide plating solution for copper-plating used on iron and steel base and preparation method thereof

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0726231B2 (en) * 1986-12-05 1995-03-22 住友金属工業株式会社 Molten salt electroplating method for steel materials
JP2000045094A (en) * 1998-07-28 2000-02-15 Sumitomo Metal Mining Co Ltd Plating method of tape-like base body
CN202090087U (en) * 2011-05-13 2011-12-28 山东建筑大学 Atomizing cleaning device for continuous copper-plating of steel strip
CN202175729U (en) * 2011-05-13 2012-03-28 山东建筑大学 Plating tank capable of continuously plating copper on steel belt
CN102605400B (en) * 2011-09-29 2014-10-08 山东建筑大学 Steel strip continuous copper plating process
CN102605399B (en) * 2011-09-29 2014-08-06 山东建筑大学 On-line recycling method for steel strip continuous copper plating
CN203159735U (en) * 2013-03-24 2013-08-28 山东建筑大学 Device for homogenizing coatings in steel strip continuous copper plating

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4050996A (en) * 1976-11-03 1977-09-27 General Motors Corporation Electochemically exchanging a steel surface with a pure iron surface
US4582573A (en) * 1985-02-25 1986-04-15 Comet Research, Inc. Method for treating a single side of a metallic sheet
CN101665962A (en) * 2009-09-04 2010-03-10 厦门大学 Alkaline non-cyanide plating solution for copper-plating used on iron and steel base and preparation method thereof

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