TW200526816A - Development and application of the silver electroplating in a cyanide-free bath at room temperature - Google Patents

Development and application of the silver electroplating in a cyanide-free bath at room temperature Download PDF

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TW200526816A
TW200526816A TW93102986A TW93102986A TW200526816A TW 200526816 A TW200526816 A TW 200526816A TW 93102986 A TW93102986 A TW 93102986A TW 93102986 A TW93102986 A TW 93102986A TW 200526816 A TW200526816 A TW 200526816A
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Taiwan
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silver
cyanide
patent application
scope
range
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TW93102986A
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Chinese (zh)
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Ching-An Huang
Shih-Chung Chen
George Chia Tu
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Ching-An Huang
Shih-Chung Chen
George Chia Tu
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Priority to TW93102986A priority Critical patent/TW200526816A/en
Publication of TW200526816A publication Critical patent/TW200526816A/en

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Abstract

In this innovation a new electrolyte composition for silver electroplating has been developed, in which we used silver halide to substitute the traditional silver cyanide used in traditional electroplating technique. In this innovation, the electrolyte composition was composed of silver chloride, lithium chloride, hydrochloride and a few EDTA or additives as the brightening agent. Silver-white colored Ag deposit could be plated onto a metallic substrate was established, such as austenitic stainless steel, copper, brass ... etc, and good adherence with the substrate. Since high purity silver deposit could be obtained by using the present electrolyte, the electroplating could be conducted at room temperature, and, the most importantly, the electrolyte employed is cyanide-free processing, the present electroplating technique is obviously suitable for high-quality silver on parts used in optical-electrical and semiconductor devices. The cyanide-free electrolyte creates a non-toxic environment, an enables safe operation which complying readily with the waste electrolyte-disposal regulations.

Description

200526816 玖、發明說明 (翻翻麟•翻臟2_纖、脑撕、随、麵斌讎說明) 【發明所屬之技術領域】 一種非氰常溫電鐵銀電鍍浴,應用在金屬工業之表面處理,特別是 一種常溫、低毒性的電鍍銀製程。 【先前技術】 目前工業界在電数製程巾,其電鍍錢泛使时有劇毒的氰化物 電鍍液,由於該電鍍作業必須在高達攝氏70〜80度溫度下進行,在此製 作過程中之’其電鍍_為自由氰濃度含量過高,在驗加卫過程中, 操作人員容易遭受氰巾毒的危害,並且製程後所產生的廢棄電艘液中, 亦含有相§同比例的之自由氰及氰化合物,因而在玉廠污、廢水排放的 處理上,需耗費相當可觀的設備成本(例如加熱設備、冷卻設備、廢水 排放處理…等等),否則不僅會造成環境生態的嚴重破壞(例如毒性物質 保存、廢棄電細亏染、污水排放···料),更會面臨環鮮位嚴厲的處 重則面S品關廠或遷 分,以及環侧制抗爭行為,酬增加經營成本 移的命運。不僅降低了產品的競爭力,以及消費者的認同;騎區員 作業安全及亦潛藏著不可預知的危機。 【內容】 本發明為-種非氰常溫電鑛銀電鑛浴,係將習用的電鑛液中之氛化 合物以氯化合物取代,除可避免氰中毒的危斜,並可將其麵賴程 t的作業/皿度降至至溫,完成後的電鍍銀層品質也可與習用的氰化合物 電鑛成果相勝糊銀嶋Φ繼㈣她合物附著^ 之該非氰錄讀液,可於f溫下進行電猶業,轉常_於高工業 20Q526816 安全標, 卜傭/低㈣之縣縣,娜光電料_管騎—之全金屬 止封螺母···等錢銀產品之製作。 厅應用之王至屬 由於本發明的製作過程穿 縛%、她無麵且不具危陳,在其廢 鑛液之處理上,應符合工 入L°/尾水排放的標準;對作業人員的工作安 王避免了钿作時氰中毒之危險性;對環境生態保育而言,則避免了 劇毋性的氰化合物對自顯境的迫害。此外,本發明不僅減少了其加工 過程t’作業人員所f防毒 _置成本,也減少了廢魏液及污水 排放等設備成本’不但增加了產品競爭力及公销譽,更容絲取到歐 美國家客戶及環保團體的認同。 【貫施方式】 本發明為-種非氰常溫電触電㈣,其係由2g/1〜i㈣1的銀 鹽、200g/l〜_g/1的活性傳導鹽、1〇ml/1〜5〇ml/l的、糊^ 及光澤劑’其餘則由水所組成,主要特徵在於以氯化銀或漠化銀等的銀 鹽取代氰化銀(AgCN),可以應用在常溫情況下進行電鍍銀製程,不僅降 低電鍍作業時,氰化合物對工作人員的毒害,更可以避免人員長期在高 溫情況下作業的不良影響。 茲配合第一圖圖示將本發明較佳的實施例詳細說明如下: 鍍銀前處理(步驟10):前處理為除去於基材上之氧化物、氫氧化 物或油脂; 浸酸(步驟11)之目的有二:一為除去金屬表面生成之薄氧化皮膜; 二為增加基材之表面活性,以利於電鍍銀程序; 200526816 電鍍前水洗(步驟12):除去基材上的髒污; 預鑛鎳(步驟13):銀不易附著於不錄鋼表面,故需纖錄於不鎮 鋼基材上,以增加絲基材之附著性,此外,預鑛鎳亦可增加基材 之表面活性; 預鍍鎳後水洗(步驟14):經過預錢鎳後,清洗上面的殘餘化合液; 電錢銀(步驟15):將包括銀鹽、活性傳導鹽、緩衝劑、蟄合劑、 光澤劑及水依照比_配成魏浴用的液體,液體溫度為常溫狀 態,其電解銀電鑛之電鑛參數控制在〇· 〇5〜3· _m2範圍内之糕 ^ 密度,經過5〜10分鐘的電鍍時間即可達到電鍍效果; 電艘銀後水洗(步驟16):經過電錢銀後,泰先其上的殘餘化合液; 及完成品乾燥(步驟17):經過完整的電鍵銀製程,將完成品放置 於陰//?、乾燥處等待風乾後,成品即可使用。 综上所述,當之本案所發明之非氰常溫電鍍銀電鑛浴以具有產業利 用性、新穎性與進步性,符合發明專利要件。為以上所述者,僅為本發 明之-較佳實施例而已,並非用來限定本發明實施之範圍。即凡依本發鲁 月申。月專利範圍所做的均等變化與修 【圖式簡單說明】 如月寻不盖。 各圖意義如下·· 第-圖林發明非氰常溫電鑛銀電錢浴之電鍍步驟圖 第-圖為本發明非氰常溫電鍍銀電锻浴之錢層斷面圖 第-圖為本發明非氰常溫電鑛銀電錢浴之鐘層表面形貌圖 *圖為本毛明非氰常溫電鍍銀電錢浴之成分分析圖 10200526816 发明, description of the invention (flip-flops and fouls 2_fiber, brain tearing, stubborn, face-bin 雠 description) [Technical field to which the invention belongs] A non-cyanide room temperature electric iron-silver plating bath, applied to the surface treatment of the metal industry , Especially a normal temperature, low toxicity silver plating process. [Previous technology] At present, in the industrial industry, electroplating process towels are highly toxic with cyanide electroplating solution. Because this electroplating operation must be performed at a temperature of 70 to 80 degrees Celsius, during this process, Its electroplating is because the content of free cyanide is too high. During the inspection, the operator is vulnerable to the danger of cyanogen poison, and the waste electric boat fluid produced after the process also contains the same proportion of free cyanide. And cyanide compounds, therefore, considerable waste of equipment costs (such as heating equipment, cooling equipment, wastewater discharge treatment, etc.) is required for the treatment of sewage and waste water discharge from the jade factory, or it will not only cause serious damage to the environment (for example, Preservation of toxic substances, depletion of waste electricity, sewage discharge ...), will also face severe environmental sanctions, such as closing the factory or relocating products, as well as fighting against environmental regulations, increasing operating costs. fate. Not only does it reduce the competitiveness of the product, but also the consumer's approval; the safety of the riders' operations and the potential for unpredictable crises. [Content] The present invention is a non-cyanide normal temperature electric ore silver-electricity ore bath, which replaces the conventional compounds in the electric ore liquid with chlorine compounds. In addition to avoiding the danger of cyanide poisoning, it can also be used in the process The work / plate temperature is reduced to warm, and the quality of the finished silver plating layer can also be compared with the results of conventional cyanide compounds. The non-cyanide recording solution can be used in Electricity is still carried out at f temperature, and it is normal to make _ Yugao Industrial 20Q526816 safety standard, commissioner / low-income counties, Nana Optoelectronics _ Guanqi-the production of all-metal stopper nuts and other money and silver products. The king of the hall application is due to the production process of the present invention. She is faceless and non-hazardous. In the treatment of her waste liquid, it should meet the standard of L ° / tail water discharge; The King of Work avoids the danger of cyanide poisoning during cropping; for environmental conservation, it avoids the persecution of self-exhibiting cyanide compounds by the severe cyanide compounds. In addition, the invention not only reduces the cost of anti-virus equipment installed by the operator during the processing process, but also reduces the cost of equipment such as waste Wei liquid and sewage discharge. It not only increases product competitiveness and reputation, but also allows for easy access The recognition of customers and environmental groups in Europe and the United States. [Performance] The present invention is a non-cyanide room temperature electric shock 触, which is composed of 2g / 1 ~ i〜1 silver salt, 200g / l ~ _g / 1 active conductive salt, 10ml / 1 ~ 5. ml / l, paste ^ and gloss agent 'The rest is composed of water, the main feature is to replace silver cyanide (AgCN) with silver salts such as silver chloride or desert silver, which can be applied to silver plating at room temperature. The manufacturing process not only reduces the toxicity of cyanide compounds to the workers during the plating operation, but also avoids the adverse effects of personnel working under high temperature conditions for a long time. The preferred embodiment of the present invention is described in detail with the illustration of the first figure as follows: Silver plating pretreatment (step 10): The pretreatment is to remove oxides, hydroxides or grease on the substrate; immersion in acid (step 11) The purpose is twofold: one is to remove the thin oxide film formed on the metal surface; the other is to increase the surface activity of the substrate to facilitate the silver plating process; 200526816 washing before plating (step 12): removing the dirt on the substrate; Pre-mineralized nickel (step 13): Silver is not easy to adhere to the surface of non-recorded steel, so fiber must be recorded on the base material of non-steel steel to increase the adhesion of silk substrate. In addition, pre-mineralized nickel can also increase the surface of the substrate. Active; Wash after pre-nickel plating (step 14): After the pre-nickel nickel, wash the remaining compound solution above; electro money silver (step 15): include silver salt, active conductive salt, buffer, chelating agent, gloss agent And water according to the ratio _ formulated into a liquid for the Wei bath, the temperature of the liquid is normal temperature, the electric and ore parameters of its electrolytic silver power ore are controlled within the range of 0. 〇5 ~ 3 · _m2 ^ density, after 5 ~ 10 minutes Electroplating time can achieve the effect of electroplating; Step 16): After passing the money silver, Taixian's residual compound liquid; and drying the finished product (Step 17): After the complete key silver process, place the finished product in a shaded place, wait for air drying , The finished product is ready to use. In summary, the non-cyanide room temperature electroplating silver electric ore bath invented in this case has industrial applicability, novelty, and progress, and meets the requirements of invention patents. What is described above is only the preferred embodiment of the present invention, and is not intended to limit the scope of implementation of the present invention. That is, according to Ben Fa Lu Yueshen. Equal changes and repairs in the scope of monthly patents [Simplified illustration of the drawing] The meanings of the figures are as follows:-The figure of the electroplating steps of the non-cyanide room temperature electroplating silver electric money bath invented by Tulin Surface morphology of the bell layer of a non-cyanide room temperature electro-smelting silver electric money bath

Claims (1)

200526816 申§靑專利範圍 I種非氰銀電錢液配方之組成,其係使用銀鹽之銀化合物來當作銀,且 έ有活性傳導鹽、緩衝劑、螯合劑以及光澤劑。 2·如申Μ專利範圍第丨項所述之非氰電解銀電練,其中銀電鑛液中含 有·使銀電錢液中的銀濃度在2g/l〜l〇g/l範圍内之量的銀化合物;200g/l 6〇〇g/l範圍内作為活性傳導鹽之無機鹽;以及〜5〇邊範圍内 作為緩衝劑之酸劑。 3.如申請專利範圍第!項所述之非氰電解銀電鑛液,其中2奶〜⑴奶顧 馨 内之銀鹽係擇自氯化銀、漠化銀、峨化銀、硝酸銀、氯酸銀或過氯酸銀 至少一者提供之。 4·如申請專纖11第1賴述之雜電解銀紐液,其巾作為活性傳導鹽 之無機鹽係為有機與無機鹽類以及硫代硫酸鹽類,取自氯化鋰、氯化鈉、 氯化鉀、氯化氨、俩鐘、鑛鈉、硝酸卸、硫代硫酸錢、硫代硫酸卸 以及硫代硫酸鈉,其中1種或2種以上提供之。200526816 The scope of the patent application § 靑 The composition of a non-cyano-silver electric money liquid formula, which uses silver compounds of silver salts as silver, and has active conductive salts, buffers, chelating agents and gloss agents. 2. The non-cyanide electrolytic silver electric drill as described in item 丨 of the patent application scope, wherein the silver electric ore liquid contains the silver concentration of the silver electric money liquid in the range of 2 g / l to 10 g / l. Amount of silver compound; an inorganic salt as an active conductive salt in the range of 200 g / l 600 g / l; and an acid agent as a buffering agent in the range of ~ 50. 3. If the scope of patent application is the first! The non-cyanide electrolytic silver power mineral liquid described in item 2, wherein the silver salt in 2 milk to ⑴ milk Gu Xin is selected from at least silver chloride, desertified silver, silver anthracite, silver nitrate, silver chlorate, or silver perchlorate. One provided. 4. As for the application of the special electrolytic silver electrolyte solution described in the first paragraph of the special fiber 11, the inorganic salts of the towel as the active conductive salt are organic and inorganic salts and thiosulfates, taken from lithium chloride and sodium chloride. , Potassium chloride, ammonia chloride, two minutes, sodium ore, nitric acid, thiosulfuric acid, thiosulfuric acid, and sodium thiosulfate, one or more of which are provided. 5. 如申請專利範圍第1項所述之非氰電解銀電鑛液,其中作為緩衝劑之酸 劑係為氣酸、過氯酸、硝酸、硫酸或醋酸其中丨種或2種以上提供 6. 如申請專利範圍第i項所述之非氰電解銀電題,其中作為光澤劑係為 EDTA、二硫化碳、硫尿、亞硒酸鈉、或硫代硫酸銨其中 上提供之。 1種或2種以 7·如申請專利範圍第6項所述之銀電鍍浴,其中作為伞 乍為切敵EDTA係為 鈉鹽、鉀鹽或鎂鹽其中1種或2種以上提供之。 11 200526816 8.如申請專利範圍第3項所述之非說電解銀電鐘液,其中銀鹽之含量挪 〜10g/l範圍内。 9·如申請專利範圍第4項所述之非氰電解銀電舰,其_作為活性傳導鹽 之無機鹽之含量係為200g/l〜6〇〇g/l範圍内。 10. 如申請專利範圍第5項所述之非氰電解銀電鍍液,其中作為緩衝劑之酸 劑之含量係為10ml/l〜50ml/l範圍内。 11. 如申請專利範圍第6項所述之非氰電解銀電鍍液,其中作為光澤劑之含 量係為O.lppm〜lOOppm之範圍内。 12. 如申請專利範圍第7項所述之銀電鍍浴,其中作為光澤劑之EDTA含 量係為10ml/l〜50ml/l之範圍内。 13·—種非氰電解銀電鍍方法,該方法係銀電鍍液中含有:使銀電鍍液中的 銀濃度在2g/l〜l〇g/l範圍内之量的銀化合物;2〇〇g/1〜6〇〇的範圍内作 為活性傳導鹽之無機鹽;以及l〇ml/l〜5〇ml/l範圍内作為緩衝劑之酸 劑,在溶液的pH值為1〜5 ;液溫為攝氏20〜45度;電流密度為0.05 〜3.0 A/dm2之條件下進行電解電鍍。 14.一種以如申請專利範圍第2至6項中任一項之電解銀電鍍液,應用於電 解銀電鍍製程。 續次頁(申請專利範圍頁不敷使用時’請註記並使用續頁) 125. The non-cyanide electrolytic silver power mineral fluid as described in the first item of the patent application scope, wherein the acid agent used as the buffering agent is gas acid, perchloric acid, nitric acid, sulfuric acid or acetic acid. Among them, one or two or more of them are provided. 6 . The non-cyanide electrolytic silver problem described in item i of the patent application scope, wherein the gloss agent is EDTA, carbon disulfide, thiourea, sodium selenite, or ammonium thiosulfate. One or two kinds of silver plating baths as described in item 6 of the scope of the patent application, in which the EDTA system is provided as one of two or more sodium salts, potassium salts, or magnesium salts. 11 200526816 8. The non-electrolytic electrolytic silver electric clock liquid described in item 3 of the scope of patent application, wherein the content of silver salt is within the range of ~ 10g / l. 9. The non-cyanide electrolytic silver electric ship described in item 4 of the scope of the patent application, the content of the inorganic salt as the active conductive salt is in the range of 200 g / l to 600 g / l. 10. The non-cyanide electrolytic silver plating solution as described in item 5 of the scope of the patent application, wherein the content of the acid agent as a buffering agent is in the range of 10 ml / l to 50 ml / l. 11. The non-cyanide electrolytic silver electroplating solution as described in item 6 of the scope of patent application, wherein the content as a glossing agent is in the range of 0.1 ppm to 100 ppm. 12. The silver plating bath described in item 7 of the scope of the patent application, wherein the content of EDTA as a glossing agent is in the range of 10ml / l to 50ml / l. 13. · A non-cyanide electrolytic silver plating method, the method is that the silver plating solution contains: a silver compound in an amount such that the silver concentration in the silver plating solution is in the range of 2 g / l to 10 g / l; 200 g In the range of / 1 to 600, it is used as an inorganic salt of active conductive salt; and in the range of 10 ml / l to 50 ml / l, it is used as an acid buffering agent, the pH value of the solution is 1 to 5; liquid temperature Electrolytic plating is performed at a temperature of 20 to 45 degrees Celsius and a current density of 0.05 to 3.0 A / dm2. 14. An electrolytic silver plating solution according to any one of claims 2 to 6 of the scope of application for a patent, applied to an electrolytic silver plating process. Continued page (if the patent application page is insufficient, please note and use the continuation page) 12
TW93102986A 2004-02-10 2004-02-10 Development and application of the silver electroplating in a cyanide-free bath at room temperature TW200526816A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI513864B (en) * 2012-01-18 2015-12-21 Metalor Technologies Japan Corp Preparation method of non - cyanide electrolytic gold plating bath and gold bump for forming gold bump

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI513864B (en) * 2012-01-18 2015-12-21 Metalor Technologies Japan Corp Preparation method of non - cyanide electrolytic gold plating bath and gold bump for forming gold bump

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