TW555890B - A metallic anode oxidation treatment system utilizing a vibration flow agitation - Google Patents

A metallic anode oxidation treatment system utilizing a vibration flow agitation Download PDF

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Publication number
TW555890B
TW555890B TW089105542A TW89105542A TW555890B TW 555890 B TW555890 B TW 555890B TW 089105542 A TW089105542 A TW 089105542A TW 89105542 A TW89105542 A TW 89105542A TW 555890 B TW555890 B TW 555890B
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Taiwan
Prior art keywords
vibration
bath
vibrating
generating mechanism
flow stirring
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TW089105542A
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Chinese (zh)
Inventor
Ryushin Omasa
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Japan Techno Co Ltd
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Priority claimed from JP11096832A external-priority patent/JP3046594B1/en
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Publication of TW555890B publication Critical patent/TW555890B/en

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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C24/00Coating starting from inorganic powder
    • C23C24/02Coating starting from inorganic powder by application of pressure only
    • C23C24/06Compressing powdered coating material, e.g. by milling

Abstract

An object of the present invention is to provide an anode oxidation method with higher anodizing rate, less energy consumption and higher efficiency of oxide film formation and to provide an anodizing method in which an excellent, uniform oxide film can be obtained without burning of the metal body even if the metal body has a complicated profile. This invention provides a metal anode oxidation treatment system, which is characterized in that, in the metal anode oxidation process, (A) is disposed with vibration generation mechanism containing vibration motor; a vibration fluidly stirring mechanism coupled with the vibration generation mechanism and one-section or multiple-sections vibration vanes fixed with a vibration rod in the stirring tank vibrating at an amplitude from 0.5 to 3.0 mm and at a vibration frequency of 200 to 800 times per minute; an AC/DC shifter used to control the vibration motor vibrating arbitrarily at 10-500 Hz; and a vibration fluidly stirring device of the treatment bath of the vibration stress distribution mechanism disposed at the connection portion of the vibration generation mechanism and the vibration fluidly stirring mechanism, and (b) is to concurrently perform an aeration in the treatment bath by using air bubbles generated by a ceramic diffuser having a pore diameter of 10 to 400 mum and 30-40% of porosity.

Description

555890 A7555890 A7

555890 經濟部智慧財產局員工消費合作社印製 A7 五、發明說明(2) 於系統外,不能有效地形成氧化膜之點而言與只使用⑺) 時無顯著之差異,不能完成「處理高速化」&「處理溫度 在比室溫高之溫度實施」之課題。又,該等氧氣氣泡化; 致被處理物表面之電阻變大,雲里古带辭 而要回電壓,其結果變成大 容量之電量伴隨著高熱,能量耗指*而 此置牦損大而且電流密度最多只 能達到2至3A/dm2 〇 [發明所欲解決之課題] 本發明之目的為提供可使銘等金屬之陽極氣化高速 化、能節省能源,同時亦可提高膜生成效率、即使在具有 複雜形狀之物品亦可形成不會燒焦、品質高且均一之陽極 氧化膜之方法。 [解決課題之方法] 本發明第一態樣係有關金屬之陽極氧化處理系統,其 特徵為:於金屬陽極氧化工序中,使 (A) 設有:包含振動馬達之振動產生機構;與振動產生 機構連動而使一段或多段固定於在攪拌槽内振動之振動捧 上之振動葉片,以振幅為0.5至3.0mm、振動數為200至 8〇〇次/分產生振動流動之振動流動攪拌機構;用以控制振 動馬達使之可在10至500Hz之間任意振動之直流交流變 換器;及設於振動產生機構與上述振動流動攪拌機構的連 接部之振動應力分散機構之對處理浴的振動流動攪拌裝 置、 (B) 作為對處理浴之充氣裝置之使用氣孔徑為1〇至 4〇〇 V m、氣孔率為30至40%之陶瓷製散氣管之充氣裝置, 卜^尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) \-- m J --------^---------^9— (請先閱讀背面之注意事項再填寫本頁) A7555890 Printed A7 by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. 5. Description of the invention (2) There is no significant difference between the point that the oxide film cannot be effectively formed outside the system and that when only ⑺ is used. "&Amp;" The treatment temperature is implemented at a temperature higher than room temperature. " In addition, the oxygen gas bubbles; the resistance of the surface of the object to be treated becomes large, and the voltage in the cloud is reciprocated. As a result, a large amount of electricity is accompanied by high heat, and the energy consumption is high. The current density can only reach 2 to 3A / dm2 at most. [The problem to be solved by the invention] The purpose of the present invention is to provide a high-speed anode gasification of metals such as Ming, which can save energy, and at the same time improve the film production efficiency, A method of forming an anodized film which is non-scorching, high quality and uniform even on articles with complex shapes. [Method for solving the problem] The first aspect of the present invention relates to an anodic oxidation treatment system for a metal, which is characterized in that: (A) is provided with: a vibration generating mechanism including a vibration motor; and Vibration flow stirring mechanism that causes one or more sections to be fixed on the vibration blades vibrating in the vibration tank in the mixing tank to generate vibration flow with an amplitude of 0.5 to 3.0 mm and a vibration number of 200 to 8000 times / minute; A DC-AC converter for controlling a vibration motor so that it can vibrate arbitrarily between 10 and 500 Hz; and a vibration flow stirring of a processing bath provided by a vibration stress dispersing mechanism provided at a connection portion between the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism Device, (B) As an inflatable device for the treatment bath, an inflatable device using a ceramic diffuser with an air pore size of 10 to 400 V m and a porosity of 30 to 40%. The dimensions are applicable to Chinese national standards ( CNS) A4 specification (210 X 297 mm) \-m J -------- ^ --------- ^ 9— (Please read the precautions on the back before filling this page) A7

555890 五、發明說明(l) 同時動作。 本發明為如前所述經由(A)之振動流動攪拌及(B)之充 氣組合進行陽極氧化,與以往只用充氣(B)之技術相比較, 電流密度可容易地上昇,進行陽極氧化處理,電流密度可 由以往方法之約2至3A/dm2變為約1〇至l5A/dm2,其結 果’處理時間可驚人地短縮。 %極氧化處理之處理溫度為能源成本及氧化膜品質極 重要之因素。在以往只用充氣(B)之方法,為了形成硬質耐 酸銘’其處理溫度需在·5至〇°C,即使形成一般之耐酸鋁 亦以在20°C以下之溫度較理想,若根據本發明之將(A)之 振動流動攪拌及(B)之充氣併用之方法,即使在形成硬質耐 酸銘時,處理溫度在10至20°C即可,又,形成一般之耐 酸鋁時在30至35°C即可,在冷卻能源方面可大幅度節省 能源,同時在氧化膜之品質上,處理溫度即使比以往方法 高,亦可獲得驚人之良好結果。 本發明人們首先於特公平6-71544號公報(特許第 1941498號)、特開平6-220697號公報(特許第2707530號) 中提案在電鍍槽中使用振動流動攪拌裝置。於電鑛槽中, 被電鑛之金屬形成陰極,被電鍍金屬離子在該陰極表面析 出’但是電鍍時必然地水會電解,在陰極表面產生氫,在 以往之方法,存在於陰極表面之氫會氣泡化,使電阻增大, 電流效率顯著降低’其結果使金屬離子之析出延遲,電鑛 需長時間,本發明人們於上述特公平6-71544號公報(特許 第1941498號)之技術中提案有將電鍍槽進行振動流動 1 # -------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 3 311303 555890 經濟部智慧財產局員工消費合作社印製 A7 五、發明說明(4) 掉。此時振動流動攪拌裝置之作用為將存在於陰極表面之 氣氣泡有效率地除去,對於妨礙金屬離子析出之氫氣泡可 有效率地阻止。相對地,陽極氧化經由水之電解,陽極所 集聚之羥離子經由放電分解成為氧,該氧使在陽極形成之 金屬表面氧化,使氧呈氣泡狀態,儘可能地不存在於陽極 表面。電鑛槽中振動流動攪拌裝置之作用為將存在於陰極 表面之氫氣泡除去,陽極氧化中使用振動流動攪拌裝置會 使必需殘存於陽極表面之氧氣泡氣體除去,該使用可認為 是禁忌。 然而’實際測試時發生完全預想不到之結果。亦即, 經由電解所產生之氧實質上不會氣泡化,推測在發生機之 氧的狀態可極有效率地與金屬反應,可比以往之方法更迅 速地形成細密且均一之氧化膜。此結果更令人驚奇。 本發明第二態樣係有關金屬之陽極氧化處理系統,其 特徵為:於金屬陽極氧化工序中,使 (A) 設有包含振動馬達之振動產生機構;與振動產生機 構連動而使一段或多段固定於在攪拌槽内振動之振動捧上 之振動葉片’以振幅為〇·5至3.0mm、振動數為200至800 次/分產生振動流動之振動流動攪拌機構;用以控制振動馬 達使之可在10至500Hz之間任意振動之直流交流變換 器,及設於振動產生機構與上述振動流動攪拌機構的連接 部之振動應力分散機構之對處理浴之振動流動攪拌裝置、 (B) 作為對處理浴之充氣裝置之使用氣孔徑為1〇至 4〇〇// m、氣孔率為30至40%之陶瓷製散氣管之充氣裝置、 ftm --------訂--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格⑽x 297公楚) 4 311303 555890 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 A7 B7 五、發明說明(5) (C) 用以透過垂吊有被處理物之電極棒,使用經由直流 交流變換器調節為10至60Hz之振動馬達,給予被處理物 振幅為0.5至1.0mm、振動數100至3〇〇次/分之振動之振 動裝置同時動作。 本發明第二態樣係有關金屬之陽極氧化處理系統,其 特徵為:於金屬陽極氧化工序中,使 (A) 設有:包含振動馬達之振動產生機構;與振動產生 機構連動而使一段或多段固定於在攪拌槽内振動之振動捧 上之振動葉片,以振幅為0.5至3 〇mm、振動數為2〇〇至 8〇〇次/分產生振動流動之振動流動攪拌機構;用以控制振 動馬達使之可在1〇至500Hz之間任意振動之直流交流變 換器;及設於振動產生機構與上述振動流動攪拌機構的連 接部之振動應力分散機構之對處理浴之振動流動攪拌裝 置、 (B) 作為對處理浴之充氣裝置之使用氣孔徑為1〇至 4〇〇私m、氣孔率為30至4〇%之陶瓷製散氣管之充氣裝置、 (D) 用以透過垂吊著被處理物之電極棒,給予被處理物 搖動幅為10至l〇0mm、搖動數為1〇至3〇次/分之搖動之 搖動裝置同時動作。 本發明第四態樣係有關金屬之陽極氧化處理系統,其 特徵為:於金屬陽極氧化工序中,使 、 ㈧設有:包含振動馬達之振動產生機構;與振動產生 機構連動而使-段或多段固定於在挽拌槽内振動之振動捧 振動葉片,以振幅為〇.5至3.0mm、振動數為細至 _ 家_ ($S)A4 祕(2»^^ 5 311303 --------^--------- (請先閱讀背面之注意事項再填寫本頁) 555890 A7 B7 五、發明說明(6 ) 8〇〇次/分產生振動流動之振動流動攪拌機構;用以控制振 動馬達使之可S 10至500Hz之間任意振動之直流交流變 換器’·及設於振動產生機構與上述振動流動攪拌機構的連 接部之振動應力分散機構之振動流動攪拌裝置、 (B) 作為對處理浴之充氣裝置之使用氣孔徑為⑺至 40〇vm、氣孔率為3〇至4〇%之陶瓷製散氣管之充氣裝置、 (C) 用以透過垂书著被處理物之電極棒,使用經由直流 交流變換器調節為1〇至60Hz之振動馬達,給予被處理物 振幅為0.5至l.0mm、振動數1〇〇至3〇〇次/分之振動之振 動裝置、 (D) 用以透過垂吊著被處理物之電極棒,給予被處理物 搖動幅為10至l00mm、搖動數為1〇至3〇次/分之搖動之 搖動裝置同時動作。 本發明具有上述之特徵,除了陽極氧化系統外與以往 之方法相同,叹置有為了控制反應溫度之加熱裝置(冬天或 寒冷地必需)及為了除去於陽極氧化浴所產生之焦耳熱之 陽極氧化浴用冷卻裝置。 於電鍍中,對於從陽極產生金屬離子,在陰極形成之 被電鍍物’該金屬離子沉著,形成金屬包覆膜由於本發 明為陽極氧化,被處理物進行電鑛時相反地形成陽極,經 由從該陽極所產生之氧自行氧化,於作為陽極之銘或其合 金之金屬表面形成氧化膜。兩者之技術思想根本上相異。 本發明中上述(Α)之對處理浴之振動流動攪拌裝置以 Φ匕各振動馬達之振動產生機構;與振動產生機構連動 311303 請 訂 ^張尺度適財國國家標^S)A4規格⑽χ挪公楚)_ 555890 A7 B7 五、發明說明(7) 而使一段或多段固定於在攪拌槽内振動之振動捧上之振動 葉片以振幅為0·5至3.〇mm、振動數為2〇〇至8〇〇次/分產 生振動流動之振動流動攪拌機構;用以控制振動馬達使之 可在10至500Hz之間任意振動,較好在3〇至6〇Hz,更 好在30至40Hz之間任意振動之直流交流變換器;及設在 振動產生機構與上述振動流動攪拌機構之連接部之振動應 力分散機構所成者較理想。振動馬達之輸出功率(w數)可 根據處理浴之液量選擇適當之輸出功率。詳細說明參照本 專利申請人們之特開平8_173785號公報[〇〇16]。 對上述處理浴之上述(B)之充氣裝置使用陶瓷製散氣 管。經由散氣管可散除在系統中所產生之焦耳熱,充氣之 機能南且合適。 於如PVC之合成樹脂管設置多數氣孔徑約lmm孔之 散氣管,空氣粒子太大,不能有效地除去電解熱且電阻會 產生偏差。本發明所使用之充氣裝置由於使用陶瓷製多孔 管作為散氣管,可解除上述之問題。上述陶瓷製多孔管以 如商品名為阿朗達姆之氧化鋁磨粒作為骨材之高溫燒成陶 瓷管較理想,陶瓷製散氣管之氣孔徑為10至400 vm,尤 其以10至120/zm較理想,氣孔率(對於表面積之比率)以 約30至40%較理想。 陶竟氣散氣管之内徑通常為50至i〇〇mm,長度與處 理浴之長度接近,通常約為1000至15〇〇mm。 設置之方法並無特別限制,使用複數支時,經由充氣 所產生之氣泡如被處理物均一圍繞似地由陶瓷製散氣管吸 本紙張尺度適用中國國家標準(CNS)A4規格⑵〇 χ 297公髮 7 311303 555890 A7 經濟部智慧財產局員工消費合作社印製 五、發明說明(8 ) 取。散氣管與散氣管平行並列時之間隔以1〇〇至l2〇mni較 理想。散氣管與被處理物間垂直方向之間隔通常以1〇〇至 300mm較理想。只要將各個條件妥善設定,充氣可比以往 之充氣強化約2倍。 作為上述(C)之必要條件之用以給予電極棒振動之振 動馬達之Hz數相對於(A)之振動馬達之Hz數為50至65% 較理想,該Hz數為1〇至60Hz,較好為20至3 5Hz,振幅 為0.5至l.〇mm。該振動是使被處理物振動而不是使處理 液流動。 作為上述(D)之必要條件之透過垂吊有被處理物之電 極棒使被處理物搖動,其搖動幅為10至100mm,較好為 20至60mm,搖動數以約10至30次/分較理想。 作為本發明對象之金屬可列舉鋁、其合金、鎂、其合 金、鈦、其合金、銳、其合金、组、其合金、锆、其合金、 鋅、其合金等。 本發明中之鋁合金只要是經由陽極氧化形成陽極氧化 膜之合金即可。具體例可列舉鋁-矽(Al-Si)、鋁-鎂(A1-Mg)、鋁-鎂-矽(Al_Mg-Si)、鋁-辞(Al-Zn)等之合金。 為了將該等金屬進行陽極氧化處理設置有公知之前處 理工序。前處理工序可列舉下述6種。 (1) 脫脂-水洗 (2) 脫脂-水洗(-蝕刻-水洗)_去污-水洗 (3) 機械拋光-脫脂-水洗 (4) 機械拋光-脫脂-水洗-蝕刻-水洗-去污-水洗 表紙張尺度適用中國國家標準(CNS)A4規格(210 x 297公爱) 8 311303 (請先閱讀背面之注意事項再填寫本頁) ▼裝--------訂·1 ΊΊΊΊΦΤ555890 V. Description of the invention (l) Simultaneous actions. According to the present invention, as described above, the anodization is performed by the vibration flow stirring of (A) and the aeration combination of (B). Compared with the conventional technology using only aeration (B), the current density can be easily increased and anodization treatment is performed. The current density can be changed from about 2 to 3 A / dm2 in the conventional method to about 10 to 15 A / dm2. As a result, the processing time can be shortened surprisingly. The processing temperature of% polar oxidation treatment is a very important factor for energy cost and oxide film quality. In the past, only the method of aeration (B) was used. In order to form a hard acid-resistant inscription, its processing temperature must be in the range of 5 to 0 ° C. Even if it is a general acid-resistant aluminum, the temperature is preferably below 20 ° C. Invented the method of using (A) vibrational flow stirring and (B) aeration, even when forming a hard acid-resistant inscription, the processing temperature can be 10 to 20 ° C, and the general acid-resistant aluminum is 30 to 30 It can be 35 ° C, which can greatly save energy in terms of cooling energy. At the same time, in terms of the quality of the oxide film, even if the processing temperature is higher than the conventional method, amazingly good results can be obtained. The present inventors first proposed the use of a vibration flow stirring device in a plating tank in Japanese Patent Publication No. 6-71544 (Patent No. 1941498) and Japanese Patent Laid-Open Publication No. 6-220697 (Patent No. 2707530). In the electric ore tank, the metal to be mined forms a cathode, and the metal ions to be plated out on the surface of the cathode. However, water must be electrolyzed during electroplating to generate hydrogen on the surface of the cathode. In the conventional method, hydrogen existing on the surface of the cathode It will bubble, increase the resistance, and significantly reduce the current efficiency. As a result, the precipitation of metal ions is delayed, and electricity ore takes a long time. The present inventors have described the technique in the aforementioned Japanese Patent Publication No. 6-71544 (Patent No. 1941498). The proposal is to make the plating tank vibrate and flow 1 # ------------------- Order --------- (Please read the precautions on the back before filling in this Page) Printed by the Intellectual Property Bureau Employees 'Cooperatives of the Ministry of Economics This paper is printed in accordance with the Chinese National Standard (CNS) A4 (210 X 297 mm) 3 311303 555890 Printed by A7 Employees' Cooperatives of the Intellectual Property Bureau of the Ministry of Economics 4) Drop. At this time, the function of the vibrating flow stirring device is to effectively remove the air bubbles existing on the surface of the cathode, and to effectively prevent the hydrogen bubbles that hinder the precipitation of metal ions. In contrast, anodization is through the electrolysis of water, and the hydroxyl ions collected in the anode are decomposed into oxygen through discharge. This oxygen oxidizes the metal surface formed on the anode, making oxygen in a bubble state, and does not exist on the anode surface as much as possible. The function of the vibration flow stirring device in the electric ore tank is to remove the hydrogen bubbles existing on the surface of the cathode. The use of the vibration flow stirring device in the anodization will remove the oxygen bubble gas that must remain on the surface of the anode. This use can be considered as a taboo. However, completely unexpected results occurred in the actual test. That is, the oxygen generated by the electrolysis does not substantially bubble, and it is estimated that the state of the oxygen in the generator can react with the metal extremely efficiently, and a fine and uniform oxide film can be formed more quickly than the conventional method. This result is even more surprising. The second aspect of the present invention relates to an anodic oxidation treatment system for a metal, which is characterized in that: (A) is provided with a vibration generating mechanism including a vibration motor in the metal anodizing process; and one or more sections are linked with the vibration generating mechanism. A vibrating flow stirring mechanism fixed on a vibrating blade that vibrates in a stirring tank generates a vibration flow with an amplitude of 0.5 to 3.0 mm and a vibration number of 200 to 800 times / minute; it is used to control the vibration motor to make it A DC-AC converter capable of arbitrarily vibrating between 10 and 500 Hz, and a vibration flow stirring device for a processing bath provided in a vibration stress dispersing mechanism provided at a connection portion between the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism, (B) as a pair Inflator for treatment bath using a ceramic diffuser with a pore size of 10 to 400 // m and a porosity of 30 to 40%, ftm -------- Order ---- ----- (Please read the precautions on the back before filling this page) This paper size is applicable to the Chinese National Standard (CNS) A4 size ⑽ x 297 Gongchu 4 311303 555890 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (5) (C) Used to suspend the electrode rod with the object to be processed, and use a vibration motor adjusted to 10 to 60Hz by a DC / AC converter, giving the object to be processed with an amplitude of 0.5 to 1.0mm 2. The vibrating device with a vibration number of 100 to 300 times per minute operates simultaneously. The second aspect of the present invention relates to an anodic oxidation treatment system for a metal, which is characterized in that: (A) is provided with: a vibration generating mechanism including a vibration motor in the metal anodizing step; A plurality of vibration blades fixed on a vibration blade vibrating in a stirring tank, and a vibration flow stirring mechanism that generates a vibration flow with an amplitude of 0.5 to 300 mm and a vibration number of 2000 to 8000 times / minute; used for controlling A DC-AC converter capable of vibrating arbitrarily between 10 and 500 Hz by a vibration motor; a vibration flow stirring device for a treatment bath, a vibration stress dispersing mechanism provided at a connection portion of the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism, (B) Inflation device using ceramic diffuser with a pore size of 10 to 400 m and a porosity of 30 to 40% as an aeration device for the treatment bath, (D) For hanging through The electrode rod of the object to be processed is given a shaking device with a shaking range of 10 to 100 mm and a shaking number of 10 to 30 times / minute. The fourth aspect of the present invention relates to an anodic oxidation treatment system for a metal, which is characterized in that: in the metal anodizing process, a vibration generating mechanism including a vibration motor is provided; and the vibration generating mechanism is linked to make- Multiple sections are fixed to the vibrating blades vibrating in the mixing tank, with an amplitude of 0.5 to 3.0 mm and a fine number of vibrations. _ 家 _ ($ S) A4 Secret (2 »^^ 5 311303 ---- ---- ^ --------- (Please read the precautions on the back before filling out this page) 555890 A7 B7 V. Description of the invention (6) 8000 times / minute vibration flow stirring Mechanism; a DC-AC converter for controlling the vibration motor to arbitrarily vibrate between S 10 and 500 Hz ', and a vibration flow stirring device provided at a vibration stress dispersing mechanism at a connection portion between the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism (B) As an inflation device for the treatment bath, an inflation device using a ceramic diffuser with an air porosity of ⑺ to 400 vm and a porosity of 30 to 40%, (C) for penetrating through the book The electrode rod of the treatment object is adjusted to 10 to 60 through a DC / AC converter. A vibration motor of Hz, which vibrates the object to be processed with an amplitude of 0.5 to 1.0 mm and a vibration number of 100 to 3,000 times per minute, (D) an electrode rod for hanging the object to be processed The rocking device with a shaking range of 10 to 100 mm and a shaking number of 10 to 30 times per minute is simultaneously operated. The present invention has the above-mentioned features, except that the anodizing system is the same as the conventional method. A heating device (required in winter or cold) for controlling the reaction temperature and a cooling device for the anodizing bath for removing Joule heat generated in the anodizing bath are provided. In electroplating, metal ions generated from the anode are formed on the cathode. The object to be electroplated, the metal ions are deposited to form a metal coating film. Since the present invention is anodized, the object to be treated is electro-mineralized to form an anode on the contrary. It is self-oxidized by the oxygen generated from the anode. An oxide film is formed on the metal surface of the alloy. The technical ideas of the two are fundamentally different. In the present invention (A), the vibration flow stirring device for the processing bath is divided into two parts. The vibration generating mechanism of the vibration motor; linked with the vibration generating mechanism 311303 Please order ^ Zhang size is suitable for the national standard of the country ^ S) A4 specifications ⑽ χNuo Chu Chu) 555890 A7 B7 V. Description of the invention (7) and fixed one or more sections A vibrating flow stirring mechanism that generates a vibrating flow at a vibration blade vibrating in a stirring tank with an amplitude of 0.5 to 3.0 mm and a number of vibrations of 2000 to 8000 times / min; used to control A vibration motor allows it to vibrate arbitrarily between 10 and 500 Hz, preferably between 30 and 60 Hz, and more preferably between 30 and 40 Hz; a DC-AC converter; and a vibration generating mechanism provided with the vibration flow The vibration stress dispersing mechanism of the connection part of the stirring mechanism is ideal. The output power (w number) of the vibration motor can be selected according to the liquid volume of the treatment bath. For details, refer to Japanese Patent Application Laid-Open No. 8-173785 [0016]. A ceramic diffuser was used for the aeration device (B) in the treatment bath. The Joule heat generated in the system can be dissipated through the air diffusing tube, and the function of inflation is south and suitable. The majority of diffuser tubes with air holes of about 1 mm are installed in synthetic resin tubes such as PVC. The air particles are too large to effectively remove the electrolysis heat and the resistance will vary. Since the inflator used in the present invention uses a porous tube made of ceramics as a diffuser, the above problems can be solved. The above-mentioned ceramic porous tube is preferably a high-temperature-fired ceramic tube such as alumina abrasive particles with a trade name of Arendam as a bone material. The air pore diameter of the ceramic diffuser tube is 10 to 400 vm, especially 10 to 120 / The zm is ideal, and the porosity (ratio to surface area) is preferably about 30 to 40%. The inner diameter of the Tao Jingqi diffuser is usually 50 to 100 mm, and the length is close to the length of the treatment bath, usually about 1000 to 1 500 mm. There is no particular limitation on the setting method. When using a plurality of branches, the air bubbles generated by inflation are uniformly surrounded by a ceramic diffuser as if to be treated. The paper dimensions are applicable to China National Standard (CNS) A4 specifications ⑵χχ297 Issue 7 311303 555890 A7 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs V. Invention Description (8) Taken. When the air diffusing tube is parallel to the air diffusing tube, the interval is preferably 100 to 120 mm. The vertical distance between the air diffuser and the object to be processed is usually preferably 100 to 300 mm. As long as each condition is properly set, the inflation can be strengthened about twice as much as in the past. As a necessary condition of the above (C), the number of Hz of the vibration motor used to vibrate the electrode rod is preferably 50 to 65% of the number of Hz of the vibration motor of (A), and the number of Hz is 10 to 60 Hz. It is preferably 20 to 35 Hz, and the amplitude is 0.5 to 1.0 mm. This vibration is to vibrate the object to be processed, rather than to flow the processing liquid. As a necessary condition of the above (D), the object to be processed is shaken by hanging the electrode rod with the object to be processed, and the shaking range is 10 to 100 mm, preferably 20 to 60 mm, and the number of shaking is about 10 to 30 times / minute. More ideal. Examples of the metal subject to the present invention include aluminum, its alloy, magnesium, its alloy, titanium, its alloy, sharp, its alloy, group, its alloy, zirconium, its alloy, zinc, and its alloy. The aluminum alloy in the present invention may be any alloy that forms an anodized film through anodization. Specific examples include alloys such as aluminum-silicon (Al-Si), aluminum-magnesium (A1-Mg), aluminum-magnesium-silicon (Al_Mg-Si), and aluminum-zinc (Al-Zn). In order to perform anodizing treatment on these metals, a known pre-treatment step is provided. Examples of the pretreatment process include the following six. (1) Degreasing-washing (2) Degreasing-washing (-etching-washing) _decontamination-washing (3) mechanical polishing-degreasing-washing (4) mechanical polishing-degreasing-washing-etching-washing-decontamination-washing The paper size of the table applies to the Chinese National Standard (CNS) A4 specification (210 x 297 public love) 8 311303 (Please read the precautions on the back before filling in this page) ▼ Packing -------- Order · 1 ΊΊΊΊΦΤ

......I 555890 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(9 ) (5) 脫脂-水洗-電解抛光或化學抛光-水洗-除去氧化物 或去污-水洗 (6) 機械抛光-脫脂-水洗-電解拋光或化學拋光-水洗-除去氧化物或去污-水洗 包括使鋁或其合金陽極氧化之前處理及後處理之各處 理工序、試藥、處理條件之一例如下表1所示。 [表1] 工 序_試 藥_處 理條件 (1)脫脂 溶劑脫脂 40〇C、 5分11 (2)水洗 水 室溫、 1分 (3)蝕刻 NaOH(50g/L) 室溫、 5分12 (4)水洗 水 室溫、 1分 (5)去污 HN〇3(5%) 室溫、 1分 (6)水洗 水 室溫、 1分 (7)陽極氧化 H2S04(200g/L) 室溫、 5分13 (8)水洗 水 室溫、 1分 (9)封孔處理 純水(沸騰水)浸潰 95〇C、 15分 (10)乾燥 自然乾燥、 10分 1 / -------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 9 311303 1 1脫脂方法亦可用有機溶劑(例如使用揮發油)、含水界面 活性劑、酸水溶液(例如5至25 W/V%硫酸水溶液)、鹼 水溶液(例如NaOH 5至20W/V%)、磷酸鹽水溶液洗淨 或電解洗淨。 *2鹼法(例如NaOH 5至25W/V%)、磷酸鹼法(例如NaOH 3 至8W/V%、磷酸鈉5至10W/V%)、硫酸鉻鹽法等。 555890 A7... I 555890 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (9) (5) Degreasing-washing-electrolytic polishing or chemical polishing-washing-removing oxides or decontamination-washing (6) Mechanical polishing-degreasing-water washing-electrolytic polishing or chemical polishing-water washing-removing oxides or decontamination-water washing includes various processing steps, reagents, and processing conditions for anodizing or post-treatment of aluminum or its alloys An example is shown in Table 1 below. [Table 1] Process_Reagent_Processing conditions (1) Degreasing solvent degreasing 40 ° C, 5 minutes 11 (2) Washing water room temperature, 1 minute (3) Etching NaOH (50g / L) room temperature, 5 minutes 12 (4) Washing water at room temperature, 1 minute (5) Decontamination HN0 (5%) room temperature, 1 minute (6) Washing water at room temperature, 1 minute (7) Anodizing H2S04 (200g / L) Room temperature 5 minutes 13 (8) Washing water at room temperature, 1 minute (9) Sealing treatment pure water (boiling water) immersed at 95 ° C, 15 minutes (10) Dry and naturally dry, 10 minutes 1 / ----- -------------- Order --------- (Please read the precautions on the back before filling this page) This paper size applies to China National Standard (CNS) A4 specifications ( 210 X 297 mm) 9 311303 1 1 The degreasing method can also use organic solvents (such as volatile oils), aqueous surfactants, acid aqueous solutions (such as 5 to 25 W / V% sulfuric acid aqueous solution), and alkaline aqueous solutions (such as NaOH 5 to 20W). / V%), phosphate aqueous solution or electrolytic cleaning. * 2 Alkali method (for example, NaOH 5 to 25W / V%), alkali phosphate method (for example, NaOH 3 to 8W / V%, sodium phosphate 5 to 10W / V%), chromium sulfate method, and the like. 555890 A7

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A7A7

555890 五、發明說明(U) 管之充氣量就160公升之處理浴而言,以大於12〇八 分較理想。 “穴 於現狀,氣孔率為30至40%之陶竟製散氣管為最高 性能之散氣管,但是,即使是高性能之散氣管,但一支散 乳管之長度以150〇mm為限,若大於該長度,則空氣無法 均一噴出。 被處理物比一支散氣管長時,根據如第19圖散氣管之 配置,可推測陶瓷製散氣管向長度方向充氣可均一化。 如第19圖所示散氣管與散氣管之間隔fl及ρ均以約 1〇〇至120mm較理想。pi以約50mm以上較理想。由此, 處理浴内之充氣可均一化。(參照第19圖)。 本發明之陽極氧化由於氧化反應會產生反應熱,處理 液若未冷卻至某一程度,則處理液之溫度不能維持一定。 又’銘或其合金表面形成之r -八丨2〇3 · ho包覆,已知處 理液之溫度上昇連帶地所形成之膜性質惡化,又,溫度若 太低則氧化膜會破裂或有裂痕。根據本發明,與以往技術 相比較,在同溫度可形成極優越之陽極氧化膜。又,根據 本發明’與以往方法相比較,即使處理溫度高1 〇至丨5 ^, 可形成與經由以往方法所獲得之氧化膜不相上下之氧化 本發明欲形成鋁之一般氧化膜時,通常可在35 °c以 下,較好在30°C左右之室溫下進行陽極氧化,又,欲形成 鋁合金之一般氧化膜時,通常可在20°C以下,較好在15 。(:左右進行處理。欲形成硬質氧化膜時,通常在1〇至15 --------------------訂--------- (請先閱讀背面之注意事項再填寫本頁} 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 11 311303 555890 部 智 慧 ί 製 A7 五、發明說明(ι〇 °C進行陽極氧化。 本發明中為了冷卻處理液設置有冷卻裝置。冷卻裝置555890 V. Description of the Invention For the 160 litre treatment bath, the aeration volume of the (U) tube is preferably greater than 1208. "In the current situation, ceramic stomata with a porosity of 30 to 40% are actually the highest performance snorkels. However, even for high-performance snorkels, the length of a stigma tube is limited to 150mm. If it is longer than this length, the air cannot be uniformly ejected. When the object to be treated is longer than a diffuser, according to the configuration of the diffuser as shown in Fig. 19, it can be inferred that the ceramic diffuser is inflated in the longitudinal direction and can be uniformized. As shown in Fig. 19 The distance fl and ρ between the air diffuser and the air diffuser shown are preferably about 100 to 120 mm. The pi is preferably about 50 mm or more. Therefore, the inflation in the treatment bath can be uniformized (refer to FIG. 19). In the anodic oxidation of the present invention, reaction heat is generated due to the oxidation reaction. If the processing liquid is not cooled to a certain degree, the temperature of the processing liquid cannot be maintained at a certain level. In coating, it is known that the properties of the film formed by the temperature rise of the treatment liquid are deteriorated, and if the temperature is too low, the oxide film may be cracked or cracked. According to the present invention, compared with the prior art, it can form a polar Superior anodized film In addition, according to the present invention, compared with the conventional method, even if the processing temperature is 10 to 5 ^ higher, an oxidation film comparable to the oxide film obtained by the conventional method can be formed. Anodizing can usually be performed at a temperature below 35 ° C, preferably at a room temperature of about 30 ° C, and when the general oxide film of an aluminum alloy is to be formed, it can usually be below 20 ° C, preferably 15 ° C. : Left and right processing. When a hard oxide film is to be formed, it is usually 10 to 15 -------------------- Order --------- (Please Read the notes on the back before filling out this page} Printed on the paper by the Consumers' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, the paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) 11 311303 555890 Ministry of Wisdom A7 V. Description of the invention (anodic oxidation is performed at ι0 ° C. In the present invention, a cooling device is provided for cooling the treatment liquid. The cooling device

係使用一般的冷卻用熱交換機,將處理液通過該=卻裝置 進行循環較理想。 T 以銘或其合金為代表之各種金屬之陽極氧化處理液通 常使用已知之鉻酸、硼酸、硼酸銨、硫酸、磷酸、草酸、 苯續酸、胺基績酸、檸樣酸、酒石酸、甲酸、號 等酸組合而成之酸溶液。 陽極氧化後進行對成為多孔面之處理,亦即封孔處 理,本發明中亦以進行同樣之封孔處理(參照昭卩α年7 月25日日刊工業新聞社發行、「鍍金技術手冊」第 至600頁)較理想。 本發明中之封孔處理可進行例如經由水蒸氣之封孔處 理、經由金屬鹽之封孔處理、經由電極沉積塗裝之封孔處 理、使用染料、顏料之封孔處理或將該等封孔處理組合之 封孔處理。 口 本發明申請專利範圍帛1項之發明的具體例如第!至 3圖所示。帛1圖為側面圖,第2圖為正面圖第3圖為 上面圖。1為處理浴’ 4為振動馬達’ 16為振動棒,17為 振動葉片’5為陰極,6為陽極,12為進行充氣用之陶瓷 製散氣管。 第4至6圖為本發明申請專利範圍第4項之具體例。 對應申請專利範圍,必要時^中止(C)及/或⑼之裝置則亦 丨^^申I»專利範圍第1項或第2項之裝置使用。作為申 張尺度適用f國國家標準(CM·規格⑵〇 χ f ^ y 12 311303 J> --------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 555890 經濟部智慧財產局員工消費合作社印製 A7 五、發明說明(U) 請專利範圍第3項之裝置使用時,搖動裝置設置有搖動馬 達3、隨搖動馬達之搖動而搖動之搖動用支承框2及以陰 極棒支承件13固定於搖動用支承框2之兼作陰極之垂吊具 5’被處理物在電性及物理性上均牢牢地連接固定於上述兼 作陰極之垂吊具5上。至於被處理物較輕時,則設置電性 連接於陽極之支持框,再活用以導線將被處理物固定於該 支持框等之固定方法較理想。 於搖動用支承框之適當部位將用以給予搖動用支承框 2振動之振動馬達14固定,該振動馬達14之振動使承受 搖動用支承框2振動,成為將振動傳達至被處理物之構 造。 另一方面,經由搖動馬達3將搖動傳達至搖動用支承 框2,使陽極本體搖動。此時搖動之振幅為1〇至1〇〇以^、 較好為20至60mm,以10至30次/分之比率慢慢地搖動。 於該具體例,搖動方向為第4圖或第5圖之左右方向。 對於浴之振動流動攪拌裝置之一例如第7、8圖所示, 但是振動流動攪拌裝置本體並不只限於該例,可使用本發 明人們之專利申請特開平6-304461號、特開平6-312124 號(特許第2762388號)、特開平6-330395號(特許第 2992177號)、特開平8·173785號、特開平9 4〇482號公報 (特許第2911393號)及特公平6-71544號公報(特許第 1941498號)所揭示之振動流動攪拌裝置。 振動流動攪拌裝置之振動應力分散機構為例如於振動 產生裝置及振動棒之連接部之設在振動棒周圍之橡膠環, 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公爱) U 311303 -------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 555890A general cooling heat exchanger is used, and the processing liquid is preferably circulated through the cooling device. T The anodizing treatment solution for various metals represented by Ming or its alloys usually uses known chromic acid, boric acid, ammonium borate, sulfuric acid, phosphoric acid, oxalic acid, benzoic acid, amino acids, citrate, tartaric acid, formic acid Acid solution composed of acids such as,, etc. After the anodization, the porous surface is treated, that is, the sealing process. In the present invention, the same sealing process is performed (refer to the "Gold plating technology manual" issued by the Japan Industrial News Agency on July 25, 1997. To 600 pages) is ideal. The sealing treatment in the present invention can be performed, for example, by a water vapor sealing treatment, a metal salt sealing treatment, an electrode deposition coating coating, a sealing treatment using a dye or a pigment, or sealing the holes. Sealing treatment of the combination.口 The specific example of the invention in the scope of patent application of the present invention is No. 1! See Figure 3. Figure 1 is a side view, Figure 2 is a front view, and Figure 3 is a top view. 1 is a treatment bath, 4 is a vibration motor, 16 is a vibration rod, 17 is a vibration blade, 5 is a cathode, 6 is an anode, and 12 is a ceramic diffuser for inflation. Figures 4 to 6 are specific examples of item 4 of the patent application scope of the present invention. Corresponding to the scope of the patent application, if necessary, the device of (C) and / or 中 suspends the use of the device of item 1 or 2 of the patent scope. As the scale of application, the national standard of country f is applicable (CM · Specification ⑵〇χ f ^ y 12 311303 J > -------------------- Order ------ --- (Please read the precautions on the back before filling out this page) 555890 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 V. Description of the invention (U) When using the device in the scope of the patent, the shaking device is provided with The rocking motor 3, the rocking support frame 2 that shakes in accordance with the rocking of the rocking motor, and the cathode hanger 5 which is fixed to the rocking support frame 2 by the cathode rod support 13 and also serves as a cathode. The object to be processed is electrically and physically They are all firmly connected and fixed to the above-mentioned hanging hanger 5 which also serves as a cathode. When the object to be processed is light, a support frame electrically connected to the anode is provided, and then the wire is used to fix the object to the support frame, etc. The fixing method is ideal. A vibration motor 14 for giving vibration to the support frame 2 for vibration is fixed at an appropriate position of the support frame for vibration, and the vibration of the vibration motor 14 causes the support frame 2 for vibration to be vibrated to transmit vibration to Structure of the object to be processed. On the other hand, it is shaken by the swing motor 3 It is conveyed to the supporting frame 2 for shaking, and the anode body is shaken. At this time, the amplitude of the shaking is 10 to 100 to ^, preferably 20 to 60 mm, and it is slowly shaken at a rate of 10 to 30 times / minute. In this specific example, the shaking direction is the left-right direction of Fig. 4 or 5. For one of the vibrational flow stirring devices of the bath, for example, as shown in Figures 7 and 8, the main body of the vibrational flow stirring device is not limited to this example, and can be used. Patent applications of the present inventors are Japanese Patent Application No. 6-304461, Japanese Patent Application No. 6-312124 (Patent No. 2762388), Japanese Patent Application No. 6-330395 (Japanese Patent No. 2992177), Japanese Patent Application No. 8.173785, Japanese Patent Application No. 9 4 The vibration flow stirring device disclosed in 〇482 (Patent No. 2911393) and Japanese Patent Publication No. 6-71544 (Patent No. 1941498). The vibration stress dispersing mechanism of the vibration flow stirring device is, for example, a vibration generating device and a vibration rod. The rubber ring of the connecting part is set around the vibrating rod. The paper size is applicable to China National Standard (CNS) A4 (210 X 297 public love) U 311303 ---------------- --- Order --------- (Please read the notes on the back before filling (This page) 555890

五、發明說明(14) 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 311303 其長度比振動棒之直徑長,通常為振動棒直徑之3至8 且其粗度比振動棒之直徑粗1.3至3〇俾,士、甘 口 • ^ 几具以粗約1 5 至2· 5倍較理想。從另一觀點說明,振動棒之直徑為至 16mm之圓棒時橡膠環之厚度以1〇至15mm較理想,振動 棒(圓棒)之直徑為20至25mm時橡膠環之厚度以2〇至 30mm較理想。 於不使用橡膠環之案例,振動應力會集中在振動傳達 構件與振動棒接合處之附近,有振動棒容易折斷之問題, 此時若在該處插入橡膠環則可解決此問題。 上述振動葉片板之材質以使用薄金屬、具有彈力之合 成樹脂、橡膠等較理想,其厚度可為經由振動馬達之上下 振動至少可使葉片板之頭端部分呈現抖動現象(呈波浪樣 狀態)之厚度,經由此給予該等系統振動及流動。金屬振動 葉片板之材質可使用鈦、鋁、鋼、鋼鐵、不銹鋼及其合金。 合成樹脂可使用聚碳酸酯、氣乙烯類樹脂、聚丙烯等。為 了提同經由振動能源傳達之振動效果,對於厚度並無特別 限定’一般使用金屬時以0.2至2mm、使用塑膠時以0.5 至1 〇mm較理想。厚度若太厚,則振動流動攪拌之效果會 減少。 振動葉片板之材質使用具有彈性之合成樹脂、橡膠等 時’對於厚度並無特別限定,一般以1至5mm較理想,使 用金屬不銹鋼時為0.2至1mm,又以0.5 mm較理想。又, 振動板之振幅為2至30mm,較好為5至l〇mm。 對於振動軸振動葉片可安裝一段或多段。對應處理液 張尺度適用中國1S^ns)A4規格( Χ 297公爱) --------------------訂---------^9— (請先閱讀背面之注意事項再填寫本頁) 555890 B7 五、發明說明(15 ) 未又振動葉片可使用複數片。增加多段之段數時,振 動馬達之負荷會變大,且振動幅變小,振動馬達會發熱。 注 又振動葉片可相對於振動棒全部以直角安裝,並以 振動棒之直角方向為〇時在(+)或(一)之方向傾斜$至, 較好為10至20。安裝較理想(參照第7圖、第9圖)。振動 葉片固定構件與振動葉片從振動軸側面看可為一體傾斜及 /或彎曲。即使為彎曲時,亦可使全體傾斜5至⑽度,尤|| 其使傾斜10至20度較理想。 —振動葉片可經由振動葉片固定構件從上下兩面夾住, 固定於振動棒上,形成振動葉片部。 具體而a,上述振動葉片可先將振動棒切削螺紋,再 用螺絲鎖緊固定,但是以用如第9圖所示之將振動葉片Η 從上下夹住之輔助性振動葉片固定構件18、18壓住,該振 動葉片固定構件18、18用螺絲24、24鎖緊,將振動葉片 1 7固定較理想。 、 使振動葉片部傾斜及/或彎曲時,可在多數振動葉片部 中將下面之丨至2片向下傾斜及/或彎曲,其他之葉片向上 傾斜及/或弯曲。經由該等操作可使處理浴底部之亦八 進行,可防止積存在底部。 又,不希望只攪拌處理浴之底部時可將上述向下彎曲 ^振動葉片拆下即可。例如沉殿物等不要之成分積存在底 部不使該等沉澱物擴散,由底部取出時較方便。又為 不使所產生之氣體太早嗔出,可使振動葉片板全都為向^ 之角度或向下彎曲。 i張尺SiT?iii^NS)A4規格⑽χ 297公髮) 311303 555890 經濟部智慧財產局員工消費合作社印製 A7 五、發明說明(1ό) 振動流動攪拌裝置可如第12圖、第13圖所示只設置 在處理浴之一邊,但是如第1至5圖所示設置於處理二之 兩邊,可對應於大型浴而使浴内均一地流動攪拌。又至 今所說明之振動流動攪拌裝置均為振動葉片上下振動型, 但是亦有本專利申請人們所提出之專利申請之如特開平 6·3〇4461號公報或第10圖、第丨丨圖所示振動方向為水平 方向、振動葉片17設置於處理浴!之底部之作法。此時以 設置於第11圖左邊之振動馬達27為中心,為了取得左邊 與右邊重量之平衡,以設置具有取得與左邊重量平衡之重 量平衡器26較理想。振動流動攪拌裝置設置於靠近處理浴 之一邊時,振動葉片之長度在浴槽較寬的方向則較長,在 浴槽較短的方向則較短,可調節流動之強度。 振動棒可與振動馬達直接連接使用,但是本發明人們 採用與發明相關之如特開平6-304461號公報或特開平6_ 330395(特許第2992177號)號公報所揭示之振動馬達之振 動經由振動框傳達至振動棒之形式。 如第9圖所示,振動葉片17與振動葉片固定構件is、 18之間若有氟素類聚合物薄膜23、23存在,則在長期使 用下可大幅度降低振動葉片之破損率,較理想。氟素類聚 合物可列舉聚四氟乙烯(PTFF)、四氟乙烯/六氟丙烯共縮聚 物(FEP)、四氟乙烯/過氟烷基乙烯醚共縮聚物(PFA)、聚氣 三氟乙烯(PCTFE)、聚偏氟乙烯(PvdF)、聚氟乙烯、乙烯/ 四氟乙稀共縮聚物(ETFE)、乙烯/氣三氟乙烯共縮聚物、丙 烯/四氟乙烯共縮聚物等,又以氟素類橡膠較理想。 --------^--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(21〇 X 297公髮) 16 311303 經濟部智慧財產局員工消費合作社印製 555890 A7 ------B7 五、發明說明(π) 本發明中陽極氧化處理浴可採用設置有上述(A)、(Β) 之裝置’上述(A)、(B)、(C)之裝置,上述(A)、(B)、(D) 之裝置或上述(A)、(Β)、(〇、(D)之裝置,將被處理物以 每一定時間在各處理浴移動之連續及/或自動系統。用於前 處理或後處理各處理浴所要求之浴以至少使用上述(A)之 裝置較理想,若將(A)+ (B)、(A)+ (B)+ (C)、(A)+ (B) + (D)或(A)+ (B) + (C) + (D)組合使用當然有效。 在前處理工序或後處理工序所要求之工序中可使用上 述之(A)、(A)+(B)、(A)+(B)+(C)、(A)+(B)+(D)或(A) + (B)+(C)+(D)之裝置,尤其在選自由脫脂工序、電解拋 光及化學抛光所成組群之抛光工序、熱水封孔處理工序之 至少一個工序中使用較理想。即使在任何一個工序使用亦 可分別提面該工序之效率。 電解拋光不使用(A)之振動流動攪拌裝置時,浴組成若 使用 碟酸(H3P〇4)(89%水溶液) 600公克/公升 硫酸(H2S04) 400公克/公升 甘油 公克/公升 則在電流密度為10至16A/d m2、電壓為5至20V、處 理溫度為90至100 °C下需1〇至15分鐘,而電解抛光使用 (A)之振動流動攪拌裝置時,則浴組成為 磷酸(89%) 300公克/公升 硫酸 200公克/公升 甘油 1 〇公克/公升 Φ t -------------------訂---------^^^1 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公爱) 17 311303 555890 A7V. Description of the invention (14) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs, 311303. Its length is longer than the diameter of the vibrating rod, usually 3 to 8 in diameter and its thickness is 1.3 to 3 in thickness. Hey, Shi, Gankou • ^ Several are ideally about 1 to 2.5 times thick. From another point of view, when the diameter of the vibrating rod is 16 to 16 mm, the thickness of the rubber ring is preferably 10 to 15 mm. When the diameter of the vibrating rod (round rod) is 20 to 25 mm, the thickness of the rubber ring is 20 to 30mm is ideal. In the case where a rubber ring is not used, the vibration stress is concentrated near the joint between the vibration transmitting member and the vibrating rod, and there is a problem that the vibrating rod is easily broken. At this time, if a rubber ring is inserted there, the problem can be solved. The material of the above-mentioned vibrating blade plate is preferably thin metal, elastic synthetic resin, rubber, etc., and its thickness may be such that at least the head end portion of the blade plate is shaken by the vibration of the vibration motor up and down (in a wave-like state) The thickness of these systems imparts vibration and flow to these systems. Metal Vibration Blades can be made of titanium, aluminum, steel, steel, stainless steel and their alloys. Examples of the synthetic resin include polycarbonate, vinyl resin, and polypropylene. In order to improve the vibration effect transmitted by the vibration energy source, there is no particular limitation on the thickness. 'Generally, it is 0.2 to 2 mm when using metal and 0.5 to 10 mm when using plastic. If the thickness is too thick, the effect of vibrational flow stirring will be reduced. When the material of the vibrating blade plate is made of elastic synthetic resin, rubber, etc., there is no particular limitation on the thickness. Generally, it is preferably 1 to 5 mm, and when metal stainless steel is used, it is 0.2 to 1 mm, and 0.5 mm is more preferable. The amplitude of the vibration plate is 2 to 30 mm, preferably 5 to 10 mm. One or more sections can be installed for the vibration shaft. Corresponding to the scale of the processing liquid, China's 1S ^ ns) A4 specification (X 297 public love) -------------------- Order --------- ^ 9— (Please read the notes on the back before filling out this page) 555890 B7 V. Description of the invention (15) Multiple blades can be used without vibrating. When the number of multi-stages is increased, the load of the vibration motor becomes larger, and the vibration amplitude becomes smaller, and the vibration motor generates heat. Note The vibrating blades can be installed at right angles to the vibrating rod, and when the right-angle direction of the vibrating rod is 0, they are inclined in the direction of (+) or (a), preferably 10 to 20. Ideal installation (refer to Figures 7 and 9). The vibrating blade fixing member and the vibrating blade may be inclined and / or bent integrally as viewed from the side of the vibrating shaft. Even when it is curved, the entire tilt can be 5 to ⑽ degrees, especially || It is ideal to tilt 10 to 20 degrees. —The vibration blade can be clamped from the upper and lower sides via the vibration blade fixing member, and fixed to the vibration rod to form a vibration blade portion. Specifically, a. The above-mentioned vibrating blade can be cut by threading the vibrating rod, and then locked and fixed with screws. When pressed, the vibration blade fixing members 18 and 18 are locked with screws 24 and 24, and the vibration blade 17 is preferably fixed. When tilting and / or bending the vibration blade portion, in most of the vibration blade portions, tilt and / or bend the two pieces below, and tilt and / or bend the other blades upward. Through these operations, the bottom of the treatment bath can be performed to prevent accumulation in the bottom. Moreover, it is not desirable to remove the above-mentioned downwardly-bending vibration blade when only the bottom of the treatment bath is stirred. For example, Shen Dianwu and other unwanted components accumulate in the bottom to prevent the sediment from spreading, and it is more convenient to remove it from the bottom. In addition, in order not to let out the generated gas too early, the vibration blade plates can all be bent at an angle of ^ or downward. i Zhang Ji SiT? iii ^ NS) A4 specifications ⑽χ 297 issued) 311303 555890 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 V. Description of the invention (1) The vibration flow stirring device can be as shown in Figures 12 and 13 The illustration is only provided on one side of the treatment bath, but as shown in Figs. 1 to 5 on both sides of the treatment bath, the bath can be uniformly flowed and stirred in accordance with a large bath. The vibrating flow stirring devices described so far are all vibrating blade up-and-down vibration types, but there are also patent applications such as Japanese Unexamined Patent Publication No. Hei 6.304461 or Figure 10 and Figure 丨 丨The vibration direction is shown in the horizontal direction, and the vibration blade 17 is installed in the treatment bath! The bottom of it. At this time, the vibration motor 27 provided on the left side of FIG. 11 is used as the center. In order to obtain the balance between the left and right weights, it is desirable to provide a weight balancer 26 having a balance with the left weight. When the vibration flow stirring device is arranged near one side of the treatment bath, the length of the vibration blade is longer in the wider direction of the bath, and shorter in the shorter direction of the bath, and the intensity of the flow can be adjusted. The vibrating rod can be directly connected to the vibration motor, but the inventors have adopted the vibration related to the invention as disclosed in JP-A-6-304461 or JP-A-6-330395 (Patent No. 2992177) via the vibration frame. Communication to the form of a vibrating rod. As shown in FIG. 9, if there are fluorine-based polymer films 23 and 23 between the vibration blade 17 and the vibration blade fixing members is and 18, the damage rate of the vibration blade can be greatly reduced under long-term use, which is ideal. . Examples of the fluorine-based polymer include polytetrafluoroethylene (PTFF), tetrafluoroethylene / hexafluoropropylene copolycondensate (FEP), tetrafluoroethylene / perfluoroalkyl vinyl ether copolycondensate (PFA), and polytrifluoroethylene Ethylene (PCTFE), polyvinylidene fluoride (PvdF), polyvinyl fluoride, ethylene / tetrafluoroethylene copolycondensate (ETFE), ethylene / gas trifluoroethylene copolycondensate, propylene / tetrafluoroethylene copolycondensate, etc., A fluorine-based rubber is also preferable. -------- ^ --------- (Please read the notes on the back before filling out this page) This paper size is applicable to China National Standard (CNS) A4 specification (21〇X 297) ) 16 311303 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 555890 A7 ------ B7 V. Description of the invention (π) In the present invention, the device provided with the above (A) and (B) can be used 'The devices of (A), (B), (C) above, the devices of (A), (B), (D) or the devices of (A), (B), (〇, (D) above, will Continuous and / or automatic system for the object to be moved in each treatment bath at a certain time. It is ideal to use at least the device of (A) above for the baths required for each treatment bath before or after treatment. If (A ) + (B), (A) + (B) + (C), (A) + (B) + (D), or (A) + (B) + (C) + (D) are of course effective. The above-mentioned (A), (A) + (B), (A) + (B) + (C), (A) + (B) + ( D) or (A) + (B) + (C) + (D) devices, especially in the polishing process selected from the group consisting of degreasing process, electrolytic polishing and chemical polishing It is ideal to use in at least one of the processes and hot-water sealing treatment process. Even if it is used in any process, the efficiency of the process can be improved separately. When electrolytic vibration is not used (A), the composition of the bath is Using dish acid (H3P04) (89% aqueous solution) 600 g / L sulfuric acid (H2S04) 400 g / L glycerol G / L, the current density is 10 to 16A / d m2, the voltage is 5 to 20V, and the processing temperature is It takes 10 to 15 minutes at 90 to 100 ° C, and when the vibrational flow stirring device of (A) is used for electrolytic polishing, the bath composition is phosphoric acid (89%) 300 g / L sulfuric acid 200 g / L glycerol 10 G / Liter Φ t ------------------- Order --------- ^^^ 1 (Please read the precautions on the back before filling this page) Paper size applies to China National Standard (CNS) A4 (210 X 297 public love) 17 311303 555890 A7

五、發明說明(18) 經濟部智慧財產局員工消費合作社印製 除了濃度可降低之外,處理溫度在50至6〇〇c即可且 處理時間亦可節省為7至i i分鐘,非常經濟。採用該等電 解抛光工序時,亦可改善所獲得氧化膜之外觀、光澤。 於化學拋光亦確認與電解拋光有相同之傾向,可大幅 度降低處理溫度之同時亦可改善所獲得氧化膜之外觀、光 澤。 [實施例] 以下列舉實施例對本發明加以說明,但是本發明並不 只限於該等實施例。本實施例均利用第1 7圖所示之系統, 當然使用第1至3圖之裝置時,則使用第17圖中及 為不存在狀態,不動作狀態。又,試驗板或試驗片尺寸小 時經由導線將試驗板或試驗片固定在連接於陽極之支持框 上。(C)及(D)之裝置對支持框動作。 實施例1 如第1至3圖所示,於進行陽極氧化之處理浴1中安 裝(A)之振動攪拌裝置及(B)之充氣裝置。各裝置之尺寸、 能力等如下所述。又,為了使處理液維持一定之溫度,以 導管連接處理浴與可冷卻處理液之冷卻用熱交換機及可汲 出處理液並使之通過冷卻用熱交換機之循環泵。 (1) 陽極氧化浴:耐熱性氣化乙烯類樹脂製寬500m、 長 750m、高 550mm (2) 振動攪拌機:如第1至2圖所示之構造日本德克能 (股)公司製造、超振動α -攪拌機3型、250Wx 200Vx 3相 振動馬達為悠拉斯振動器KEE 3.5-2B型250W、附直流交 -------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 18 311303 555890 經濟部智慧財產局員工消費合作社印製 A7 五、發明說明(D ) 流變換器(0.4KW) 振動葉片:有效面積為300x 1〇〇mm厚〇 5mm5片、 a = \5° (只有下面之一段向下,其餘均向上) 振動葉片之振幅1.5mm (3) 散氣管··曰本德克能(股)公司製造之微充氣器 BM-100、(内徑5〇mm、外徑75匪、長45〇匪)氣孔率η 至38/i、氣孔徑5〇至的“扭容積比重·· 2 2至2.5 (4) 散氣管吹氣:旋轉式氣泵、輸出功率15〇w、空氣 喷出量120公升/分 (5) %極氧化浴··收容液量16〇公升硫酸2〇〇公克/公 升、鋁4公克/公升 (6) 陰極板:銘板4片寬60mm、厚20mm、長50〇mm (7) 試驗板:與被處理物相當之純銘板(A11〇〇p、 JISH400、矽 + 鐵:i.o%以下、銅:〇 〇5 至 〇 2〇%、錳· 〇 〇5% 以下、辞:0.10%以下、銘:99.00%以上) 長 100mm、寬 100mm、厚 1.5mm (8) 試驗板吊具··用鋁線將試驗板固定於陽極框中(參 照第21圖) (9) 冷卻用熱交換器:冷襯墊自動直冷式急速冷卻裝置 4010仟卡/小時,電動機l.5kw 口徑25A昭和鉛鐵(股)公 司製 “ (10) 熱交換器用循環泵:磁鐵泵最大注量12〇公升/ 分、Max Head 8.6m、200V、輸出功率 265W、1 27A、(伊 木紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐)^ ------ 311303 --------1--------- (請先閱讀背面之注意事項再填寫本頁) 555890 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(20 ) 瓦契 MD-100RM)V. Description of the invention (18) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs In addition to reducing the concentration, the processing temperature can be 50 to 600c and the processing time can be saved to 7 to i minutes, which is very economical. When these electrolytic polishing processes are used, the appearance and gloss of the obtained oxide film can also be improved. In chemical polishing, the same tendency as that of electrolytic polishing has been confirmed. It can significantly reduce the processing temperature and improve the appearance and gloss of the obtained oxide film. [Examples] The present invention will be described below with examples, but the present invention is not limited to these examples. In this embodiment, the system shown in FIG. 17 is used. Of course, when the devices of FIGS. 1 to 3 are used, the state in FIG. 17 and the non-existing state and the inactive state are used. When the size of the test plate or test piece is small, the test plate or test piece is fixed to a support frame connected to the anode via a wire. The devices of (C) and (D) act on the support frame. Example 1 As shown in Figs. 1 to 3, a vibration stirring device (A) and an aeration device (B) were installed in a treatment bath 1 for anodizing. The dimensions, capabilities, etc. of each device are described below. In order to maintain a constant temperature of the processing liquid, the processing bath is connected to a cooling heat exchanger for cooling the processing liquid and a circulating pump capable of drawing out the processing liquid and passing it through the cooling heat exchanger by a pipe. (1) Anodizing bath: 500 m wide, 750 m long, and 550 mm high made of heat-resistant gasified vinyl resin. (2) Vibration stirrer: Structure shown in Figure 1 to 2. Vibration α-Mixer type 3, 250Wx 200Vx 3-phase vibration motor is a Ulas vibrator KEE 3.5-2B type 250W, with DC AC ------------------- Order- -------- (Please read the precautions on the back before filling this page) This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) 18 311303 555890 Employees ’Intellectual Property Bureau of the Ministry of Economy Consumption Cooperative printed A7 V. Description of the invention (D) Current transformer (0.4KW) Vibrating blade: effective area is 300x100mm thick and 5mm5 pieces, a = \ 5 ° (only the lower section is downward, the rest are all upward) ) The amplitude of the vibration blade is 1.5mm. (3) Air diffuser ·· The micro-inflator BM-100 (inner diameter: 50mm, outer diameter: 75mm, length: 45mm), air vents "Torque volume specific gravity ·· 2 to 2.5 (2) to 2 / 2.5 (4) air blower: Rotary air pump, output power 15w, air ejection volume 120 liters / (5)% polar oxidation bath ·· Containing liquid volume of 160 liters of sulfuric acid 2,000 g / liter, aluminum 4 gram / liter (6) Cathode plate: 4 pieces of nameplate 60 mm wide, 20 mm thick, and 50 mm long (7) Test plate: Pure nameplate equivalent to the object to be treated (A11〇p, JISH400, silicon + iron: 10% or less, copper: 0.05 to 0.02%, manganese · 5% or less, word: 0.10% Below, Ming: 99.00% or more) 100mm in length, 100mm in width, and 1.5mm in thickness (8) Test plate hanger · Fix the test plate to the anode frame with aluminum wire (see Figure 21) (9) Heat exchange for cooling Device: Automatic direct-cooling type rapid cooling device with cold pad 4010 kcal / hour, motor 1.5kw caliber 25A manufactured by Showa Lead Iron Co., Ltd. (10) Circulation pump for heat exchanger: magnet pump maximum injection capacity 120 liters / Min, Max Head 8.6m, 200V, output power 265W, 1 27A, (Yimu paper size applies Chinese National Standard (CNS) A4 specification (210 X 297 mm) ^ ------ 311303 ----- --- 1 --------- (Please read the notes on the back before filling out this page) 555890 Printed by A7 B7, Consumer Cooperative of Intellectual Property Bureau, Ministry of Economic Affairs 20) Vache MD-100RM)

(11) 整流器:電鍍用矽整流器額定值60V-100A、 6.0kw、交流輸入 200V、21.2A、7.34KVA(11) Rectifier: Silicon rectifier for electroplating rated 60V-100A, 6.0kw, AC input 200V, 21.2A, 7.34KVA

[超迷你直流電源裝置MB7C_6〇0-01中央製作所 (股)公司] (12) 極間距離:i〇〇mm (13 )<處理浴之配置 > 脫脂浴—水洗浴—餘刻浴—水 洗浴-去污浴—水洗浴—陽極氧化浴—水洗浴—封孔處理 浴—乾燥浴 (註)蝕刻浴:苛性鹼50公克/公升、RT5分 去污浴:硝酸5%、RT 1分 封孔處理浴:離子交換過之水之沸騰水15分 <陽極氧化條件> 振動流動攪拌之Hz數為37Hz(振動馬達250Wx 200V X 3相、直流交流變換器〇 4k w),進行浴之振動流動搜拌, 在上述充氣條件下在如第20圖0所示之電流密度使陽極電 壓為20V、處理浴之溫度為2(TC,進行陽極氧化處理8分 鐘。 經由此可獲得20/zm之陽極氧化膜,該膜細密且表面 光澤良好。該等結果如表1所示。 比較例1 -1 除了實施例1之振動攪拌裝置不動作且電流密度為 2 A/d m2之外與實施例丨相同操作,處理至陽極氧化膜之膜 厚為與實施例1相同之20 // m為止,所需要之時間為4〇 ------------*-------訂--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 20 311303 經濟部智慧財產局員工消費合作社印製 555890 A7 _ B7_ 五、發明說明(21 ) 分鐘,該結果如表2所示。 比較例 1-2 除了實施例1之振動攪拌裝置不動作、電流密度為 2 A/d m2且在陽極連接振動裝置,經由直流交流變換器調節 為40Hz,給予被處理物振幅為0.5至1.0mm、振動數為200 次/分之振動之外與實施例1相同操作,處理至陽極氧化膜 之膜厚為與實施例1相同之20 " m為止,所需要之時間為 20分鐘,該結果如表2所示。 實施例1與比較例1-1、比較例1-2之對比數值如下述 表2所示。 [表2] 電流密度 A/dm 20/z 之 時間*1 外觀 (HV)*2 _蝕性 *3 染色性 *4 财磨損性 *5 實施例1 10 8分鐘 光澤佳 430 100h 佳 1200 比較例1-1 2 40分鐘 光澤差 350 48h 稍佳 800 比較例1-2 2 20分鐘 有光澤 400 60h 稍佳 900 *1陽極氧化膜厚:以JIS H8680-1979為基準之渦電流式 測定法 *2硬度:根據JIS H8682-1988之維氏硬度計(HV)之硬質 包覆膜試驗 *3耐腐蝕性試驗:以JIS-H8681-1988、評估No.9為基準 *4染料性:食品水溶性染料紅色0.5%、JIS H8685-1988 *5耐磨損性:以JIS-H8682-1988(往返運動平面磨損試驗) 為基準但是荷重在一般陽極氧化膜時為400± 10gf(3.92土 0.09N)、在硬質陽極氧化膜時為2000± 50gf(19.6± 0.49N) 比較例1 -2不比實施例1好可認為是液體中之鋁面上 k : -------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 21 311303 555890[Ultra-Mini DC Power Supply Device MB7C_6〇0-01 Central Manufacturing Co., Ltd.] (12) Distance between electrodes: 〇〇mm (13) < Configuration of processing bath > Degreasing bath-water bath-remaining bath- Water bath-Decontamination bath-Water bath-Anodizing bath-Water bath-Sealing treatment bath-Drying bath (Note) Etching bath: Caustic 50 g / L, RT 5 minutes Decontamination bath: 5% nitric acid, RT 1 minute seal Pore treatment bath: 15 minutes of boiling water of ion-exchanged water < anodizing conditions > The number of Hz of vibration flow stirring is 37Hz (250W x 200V X 3 phase vibration, DC AC converter 0kw) Under the aerated condition, under the above-mentioned aeration condition, the anode voltage was 20V and the temperature of the treatment bath was 2 ° C under the current density as shown in FIG. 20, and anodizing treatment was performed for 8 minutes. 20 / zm was obtained by this. An anodized film, the film is fine and the surface gloss is good. These results are shown in Table 1. Comparative Example 1 -1 Except that the vibration stirring device of Example 1 does not operate and the current density is 2 A / d m2, it is implemented Example 丨 the same operation, the film thickness of the anodized film is the same as that of Example 1 Same as 20 // m, the time required is 4〇 ------------ * ------- order --------- (Please read the back first Please pay attention to this page, please fill in this page) This paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) 20 311303 Printed by the Intellectual Property Bureau Employee Consumer Cooperative of the Ministry of Economic Affairs 555890 A7 _ B7_ V. Description of the invention (21) The results are shown in Table 2. Comparative Example 1-2 Except that the vibration stirring device of Example 1 did not operate, the current density was 2 A / d m2, and the vibration device was connected to the anode, and adjusted to 40 Hz through a DC / AC converter. The same operation as in Example 1 was performed except that the amplitude of the object to be treated was 0.5 to 1.0 mm and the number of vibrations was 200 times per minute. The treatment was performed until the film thickness of the anodic oxide film was equal to 20 " m as in Example 1. The required time is 20 minutes, and the results are shown in Table 2. The comparative values of Example 1 and Comparative Example 1-1 and Comparative Example 1-2 are shown in Table 2 below. [Table 2] Current density A / dm Time at 20 / z * 1 Appearance (HV) * 2 _Corrosiveness * 3 Dyeability * 4 Financial wear * 5 Example 1 10 8 minutes gloss good 430 100h good 1200 Comparative example 1-1 2 40 minutes gloss difference 350 48h slightly better 800 Comparative Example 1-2 2 20 minutes gloss 400 60h slightly better 900 * 1 Anodized film thickness: eddy current method based on JIS H8680-1979 * 2 hardness: according to JIS H8682-1988 Vickers Hardness Tester (HV) Hard Coating Test * 3 Corrosion Resistance Test: Based on JIS-H8681-1988, Evaluation No. 9 * 4 Dyeability: Food water-soluble dye red 0.5%, JIS H8685-1988 * 5 Abrasion resistance: Based on JIS-H8682-1988 (reciprocating plane abrasion test) as the standard, but the load is 400 ± 10gf (3.92 soil 0.09N) in general anodized film, in hard anodized film At 2000 ± 50gf (19.6 ± 0.49N) Comparative Example 1 -2 is not better than Example 1 and can be considered as the aluminum surface in liquid k: ------------------ -Order --------- (Please read the precautions on the back before filling this page) This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) 21 311303 555890

經濟部智慧財產局員工消費合作社印製 比較例1之電流密度在2A/d m2停止,相對地實施例1 之電机畨度可上昇至! 〇 A/d m2,因此實施例ι之陽極氧化 速度為比較例1之約5倍,且陽極氧化膜之硬度、耐腐蝕 陡染色眭、耐磨損性之任何一項實施例1之數值均比比 較例1高。10// m、15//扭之陽極氧化膜亦獲得幾乎相同 之結果。 實施例2 與實施例1之(1)至(13)所有條件均相同,根據第1至 3圖之裝置在下述之陽極氧化條件下進行陽極氧化。 <陽極氧化條件> 振動流動攪拌之Hz數為37Hz(振動馬達150Wx 200V X 3相、直流乂流變換器〇 4kw),進行浴之振動流動攪拌, 在上述充氣條件下使陽極電壓為15V、處理浴之溫度為3〇 °C進行陽極處理5分鐘,該等結果如表3所示。 比較例2 除了實施例2之振動攪拌裝置不動作之外與實施例2 相同操作,進行陽極氧化5分鐘(比較例2-1)。相同地進行 陽極氧化至陽極氧化膜之膜厚與實施例2相同為止(比較 例2_2)。該等結果如表3所示。 比較例3 除了以於陽極連接振動裝置,經由直流交流變換器調 節為40Hz,給予被處理物振幅為〇·5至l.〇mm、振動數為| --------^— (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 22 311303 555890Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs The current density of Comparative Example 1 stops at 2A / d m2, and the motor's degree of Example 1 can be increased to relatively! 〇A / d m2, the anodic oxidation rate of Example 1 is about 5 times that of Comparative Example 1, and the hardness of the anodic oxide film, the corrosion resistance and steep dyeing, and the abrasion resistance of any of Example 1 are all It is higher than Comparative Example 1. The 10 // m, 15 // twisted anodized films also obtained almost the same results. Example 2 All conditions (1) to (13) of Example 1 are the same. Anodization was performed under the following anodizing conditions according to the apparatus of Figures 1 to 3. < Anodic oxidation conditions > The Hz number of vibration flow stirring is 37 Hz (150Wx 200V X 3-phase, DC flow converter 0kw), and the vibration flow stirring of the bath is performed, and the anode voltage is 15V under the above aeration conditions. 3. The temperature of the treatment bath was 30 ° C for 5 minutes. The results are shown in Table 3. Comparative Example 2 Anodization was performed for 5 minutes in the same manner as in Example 2 except that the vibration stirring device of Example 2 was not operated (Comparative Example 2-1). Anodization was performed in the same manner until the film thickness of the anodized film was the same as that in Example 2 (Comparative Example 2_2). These results are shown in Table 3. Comparative Example 3 Except that the vibration device was connected to the anode and adjusted to 40 Hz via a DC / AC converter, the amplitude of the object to be treated was 0.5 to 1.0 mm, and the number of vibrations was | -------- ^ — ( Please read the notes on the back before filling this page.) This paper size applies to Chinese National Standard (CNS) A4 (210 X 297 mm) 22 311303 555890

五、發明說明(23 ) [表3] 200次/分之振動取代停止實施例2中(A)之振動流動攪拌 之外與實施例2相同操作進行陽極氧化。但是,比較例3-1 為在電流密度為5A/d m2進行陽極氧化5分鐘、比較例3_2 為在電流密度為10 A/d m2進行陽極氧化10分鐘。 電流密度 A/dm 時間 溫度 膜厚 (")*1 外觀 硬度 (HV)*2 耐鹽水 喷霧*6 實施例2 15 5分鐘 30°C 15 β 有光澤 350 48h 比較例2-1 3 5分鐘 30°C 5// 不均一 330 24h 比較例2-2 3 20分鐘 30°C 15 β 一無光澤 產生裂痕 不能測定 不能測定 比較例3-1 5 5分鐘 30°C Ί β 無光澤 300 不能測定 比較例3-2 10 10分鐘 30°C 15 β 統少 320 24h *6耐鹽水喷霧:以jis K5400為基準 評估 實施例2之陽極氧化速度可達到比比較例2-2快約4 倍,可形成光澤充足且耐用之氧化膜,而在以往方法之比 較例2-1或2-2,處理浴溫度若達到30°C則不能獲得具實 用性之陽極氧化膜。 實施例3 除了實施例1中(7)之試驗板以硬質鋁板(A5052P、JIS H400、矽:〇·25%以下、鐵:0.04%以下、銅·· 0.01%、錳: 〇·〇1%以下、鎂:2.2 至 2.8%、鉻:0.15 至 0.35%、鋅:0·1〇/〇 以下)取代外依實施例1反覆操作,製作膜厚為20// m之 陽極氧化膜。該結果如表4所示。 1L較例3 除了實施例3之振動攪拌裝置不動作之外與實施例3 I------------------ C請先閱讀背面之注意事項再填寫本頁} --訂--------- 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 23 311303 555890 A7 B7 五、發明說明(24) 同樣操作,進行陽極氧化至獲得膜厚為20 之陽極氧化 膜為止。該結果如表4所示。[表4] 電流密度 A/dm 時間 膜厚*1 外觀 實施例3 比較例3 硬度 (HV)*2 耐鹽水 喷霧*6 染色性*4 耐摩損性 *5 15 3.5 8分鐘 30分鐘 2〇β 20β 光澤佳 光澤少 460 350 150h 42h 良好 稍不均 800 600 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 評t 在硬質陽極氧化時,實施例3可比比較例3快約4倍 之速度形成同一厚度之氧化膜,該氧化膜之特性、外觀、 硬度、染色性、耐摩損性均優越。 實施例4 利用實施例1之裝置,試驗板使用鋁板A5052,在電 流密度為8 A/d m2將陽極氧化處理浴之浴溫作種種變化,製 作膜厚度為1 5 " in之&極氧化膜’測定該膜厚硬度。該社 果如第16圖所示。〇為實施例4。 比較例4 除了實施例4之振動攪拌裝置不動作之外依實施例4 反覆操作(電流密度為1.5 A/d m2)。該結果如第16圖所 示。•為比較例4。 評估 與比較例4比較,判定在對應處理浴溫度相同之條件 下,實施例4包覆膜之硬度都比較高,所以,若要獲得與 比較例相同硬度之氧化膜時’處理浴溫度可比比較例高, 在冷卻能源、處理時間方面對本發明特別有利。 實施例_ 本紙張尺度適用中國國家標準(CNS)A4規格(210 x 297公釐) 24 311303 I --------訂--------- (請先閱讀背面之注意事項再填寫本頁} 555890 A75. Description of the invention (23) [Table 3] Anodization was performed in the same manner as in Example 2 except that the vibration flow stirring of (A) in Example 2 was stopped at 200 times / min. However, Comparative Example 3-1 was anodized at a current density of 5 A / d m 2 for 5 minutes, and Comparative Example 3_2 was anodized at a current density of 10 A / d m 2 for 10 minutes. Current density A / dm Time & temperature Film thickness (* quot) Appearance hardness (HV) * 2 Salt spray resistance * 6 Example 2 15 5 minutes 30 ° C 15 β Gloss 350 48h Comparative Example 2-1 3 5 Min. 30 ° C 5 // Non-uniform 330 24h Comparative Example 2-2 3 20 minutes 30 ° C 15 β A matte crack can not be measured Cannot be measured Comparative Example 3-1 5 5 minutes 30 ° C Ί β Matte 300 No Measurement Comparative Example 3-2 10 10 minutes 30 ° C 15 β system less 320 24h * 6 Salt water spray resistance: Based on jis K5400 evaluation, the anodic oxidation rate of Example 2 can be about 4 times faster than Comparative Example 2-2 An oxide film with sufficient gloss and durability can be formed. In Comparative Examples 2-1 or 2-2 of the conventional method, if the temperature of the processing bath reaches 30 ° C, a practical anodized film cannot be obtained. Example 3 Except for the test plate of (7) in Example 1, a rigid aluminum plate (A5052P, JIS H400, silicon: 0.25% or less, iron: 0.04% or less, copper ... 0.01%, manganese: 〇.01% Below, magnesium: 2.2 to 2.8%, chromium: 0.15 to 0.35%, zinc: 0.10 / 0 or less) was replaced in accordance with Example 1 to produce an anodized film having a film thickness of 20 // m. The results are shown in Table 4. 1L Comparative Example 3 Except that the vibration stirring device of Example 3 does not work and Example 3 I ------------------ C Please read the precautions on the back before filling in this Page} --Order --------- Printed by the Employees' Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs This paper is printed in accordance with China National Standard (CNS) A4 (210 X 297 mm) 23 311303 555890 A7 B7 V. (24) In the same manner, anodization is performed until an anodized film having a thickness of 20 is obtained. The results are shown in Table 4. [Table 4] Current density A / dm Time film thickness * 1 Appearance example 3 Comparative example 3 Hardness (HV) * 2 Salt spray resistance * 6 Dyeability * 4 Wear resistance * 5 15 3.5 8 minutes 30 minutes 2 β 20β Good gloss Less gloss 460 350 150h 42h Good slightly uneven 800 600 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs t In hard anodizing, Example 3 can form the same thickness about 4 times faster than Comparative Example 3 The oxide film has excellent characteristics, appearance, hardness, dyeability, and abrasion resistance. Example 4 Using the device of Example 1, an aluminum plate A5052 was used for the test plate, and the bath temperature of the anodizing treatment bath was changed at various current densities of 8 A / d m2 to produce a film thickness of 1 5 " in of & The oxide film 'measures the hardness of the film thickness. The results are shown in Figure 16. 〇 is Example 4. Comparative Example 4 The operation was repeated in accordance with Example 4 except that the vibration stirring device of Example 4 did not operate (current density was 1.5 A / d m2). The results are shown in Figure 16. • For Comparative Example 4. The evaluation is compared with Comparative Example 4, and it is determined that the hardness of the coating film of Example 4 is relatively high under the same conditions of the corresponding processing bath temperature. Therefore, if an oxide film with the same hardness as the comparative example is to be obtained, the temperature of the processing bath can be compared The example is high, and is particularly advantageous to the present invention in terms of cooling energy and processing time. Example _ This paper size applies to China National Standard (CNS) A4 (210 x 297 mm) 24 311303 I -------- Order --------- (Please read the note on the back first Matters refill this page} 555890 A7

五、發明說明(25 )V. Description of the invention (25)

7壁面部為鱗造品凹陷之L字壁部分 8底部為鱗造品凹陷之底部 與實施例1相同方法及相同裝 久々日U衣直將銘鑄造品(約150χ X 4〇mm ’多數寬為3至15mm、深約15至20mm之 不規則凹陷存在)進行陽極氧化,製作厚度為bp之陽 極氧化膜。該結果如表$所示。 比較例5 除了實施例5之振動授拌裝置不動作之外依實施例$ 反覆操作。該結果如表5所示。 [表5] 實施例5所有之凹陷部分亦都形成均一之氧化膜,比較 例5即使以實施例5之4倍處理時間,其凹陷部分之氧化 膜仍比其他部分薄很多,導至全體臈厚不均一,且氧化臈 亦沒有如實施例5之光澤。根據本發明對於具有如寬為 Wnm、深為10至15mm凹陷之製品亦有效。又實施例$ 之處理時間約為比較例5之1/4。 除了實施例5中之處理溫度改為3(rc、經由散氣管之 空氣噴出量改為240公升/分之外依實施例6反覆操作。氧 化處理膜成為15 // m之時間只需5分鐘。若在該等條件下 可進行陽極氧化,則從前處理至後處理可用傳送帶連續處 --------訂--------- (請先閱讀背面之注意事項再填寫本頁} 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公爱) 25 311303 555890 A7 B7 五、發明說明(26 ) 理,不需採用導管方式即可同樣地進行電極沉著塗裝處 理。 比較例6 除了實施例6之振動擾拌裝置不動作之外依實施例6 反覆操作。氧化膜非常不均勻,有許多凹凸,無實用性。 實施例7-1 為與第4至6圖為大型之系統相對地使用如第12至 14圖所示之小型系統之例子。於陽極氧化浴安裝振動 攪拌裝置、(B)充氣裝置、(C)為了賦予被處理物之垂吊具 搖動之裝置及(D)經由垂吊具給予被處理物振動之裝置。 又,為了使處理液維持一定之溫度,以導管連接處理浴與 可冷卻處理液之冷卻用熱交換機及可汲出處理液並使之通 過冷卻用熱交換機之循環泵。其他之條件如下所述操作進 行實驗,該結果歸納如表6。 <處理浴之配置> 脫脂浴(〇)—水洗浴—蝕刻浴—水洗浴—去污浴(〇) —水洗浴—陽極氧化浴(◎)—水洗浴—封孔處理浴(〇)— 乾燥浴。 標示◎之浴為安裝上述(A)、(B)、(C)、(D)之各裝置。 標示〇之浴為只安裝上述(A)之裝置。 又,水洗浴使用自來水(常溫)。 <被處理物(陽極)> 純銘板(500mmx 200mmx 10mm) 1 片 陽極與陰極之距離:100mm (請先閱讀背面之注意事項再填寫本頁)7 The wall face is an L-shaped wall part of the scale product depression. 8 The bottom is the scale product depression. The bottom is the same as in Example 1. An irregular pit exists between 3 to 15 mm and a depth of about 15 to 20 mm.) Anodizing is performed to produce an anodized film having a thickness of bp. The results are shown in Table $. Comparative Example 5 The operation was repeated in accordance with Example $ except that the vibration mixing device of Example 5 did not operate. The results are shown in Table 5. [Table 5] All the recessed parts of Example 5 also formed a uniform oxide film. Even in Comparative Example 5, the oxide film of the recessed parts was still much thinner than the other parts even with 4 times the processing time of Example 5, leading to the whole. The thickness was uneven and the hafnium oxide did not have the gloss as in Example 5. It is also effective according to the present invention for articles having depressions such as Wnm in width and 10 to 15 mm in depth. The processing time of Example $ is about 1/4 of that of Comparative Example 5. Except that the treatment temperature in Example 5 was changed to 3 (rc, and the amount of air sprayed through the air diffuser was changed to 240 liters / minute), the operation was repeated in accordance with Example 6. The time required for the oxidation treatment film to become 15 // m was 5 minutes. .If anodizing can be performed under these conditions, the continuous belt can be used from pre-processing to post-processing -------- order --------- (Please read the precautions on the back before filling This page} Printed by the Consumers' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs The paper size applies to the Chinese National Standard (CNS) A4 (210 X 297 public love) 25 311303 555890 A7 B7 V. Description of the invention (26) Principle, no need to use a catheter In the same manner, the electrode deposition coating process can be performed in the same manner. Comparative Example 6 Repeated operation according to Example 6 except that the vibration stirring device of Example 6 does not operate. The oxide film is very uneven, has many irregularities, and is not practical. Example 7-1 is an example of using a small system as shown in Figures 12 to 14 as opposed to the large system shown in Figures 4 to 6. Install a vibration stirring device, (B) aeration device, (C) in the anodizing bath In order to impart a swing to the object, And (D) a device for vibrating the object to be treated via a sling. In addition, in order to maintain a constant temperature of the treatment liquid, a heat exchanger for cooling the treatment bath and the cooling treatment liquid that can cool the treatment liquid are connected by a duct, and the treatment liquid can be drawn out and made It passes through the circulation pump of the cooling heat exchanger. Other conditions are used to conduct experiments as described below, and the results are summarized in Table 6. < Configuration of treatment bath > Degreasing bath (〇) —water bath—etching bath—water bath— Decontamination bath (〇)-water bath-anodizing bath (◎)-water bath-plugging treatment bath (〇)-drying bath. The bath marked with ◎ is to install the above (A), (B), (C), (D) Each device. The bath marked with “0” is only installed with the above (A). Also, tap water (normal temperature) is used for water bathing. ≪ Processed object (anode) > Pure nameplate (500mmx 200mmx 10mm) 1 piece Anode and cathode distance: 100mm (Please read the precautions on the back before filling this page)

Aw----- 11111 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 26 311303 A7Aw ----- 11111 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) 26 311303 A7

555890 五、發明說明(27) <陰極> 純銘板(500mmx 60mmx 20mm) 8 片 陽極與陰極之相關位置為陽極安裝於處理浴之中央, 處理浴兩側離開陽極l〇〇mm之位置分別安裝4支陰極(參 照第1 5圖)。以陽極之上部在液面下面7〇mm,下部在浴 底上面70mm安裝。 <用於陽極氧化之處理浴> 浴大小(内尺寸):寬50〇111111父7 5〇11111^5 5〇111111(約168 公升) 振動攪拌機 振動馬達:250Wx 200VX 3相1台(商品名悠拉斯振 動器:村上精機工作所製造、安川商業公司販售) 振動葉片:有效面積300χ 150mm、厚〇 6mm 6片、 α = 15° (只有下面之一段向下,其餘均向上) 振動葉片之振幅:1.5mm 振動頻率·· 37Hz(經由直流交流變換器調節) 充氣裝置 使用外徑為75mm、内徑為50mm、長為450mrn、氣 孔徑為約200从m之陶瓷製散氣管3支。使用每支之氣孔 率為40/〇、空氣吹出量約120公升/分、輪出功率為15〇w 之旋轉式氣泵。 搖動裝置 經由帶減速器電動機或筒式電動機以20次/分給予前 ^紙張尺度適用中國國家標準(CNS)A4規格(21〇 X 297公釐)' -- 27 311303 --------------------訂---------W&WI Γ%先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製555890 V. Description of the invention (27) < Cathode > Pure nameplate (500mmx 60mmx 20mm) 8 pieces of anode and cathode are located at the center of the treatment bath, and the two sides of the treatment bath are separated from the anode by 100mm. Install 4 cathodes (refer to Figure 15). The upper part of the anode was mounted 70 mm below the liquid surface, and the lower part was mounted 70 mm above the bath floor. < Treatment bath for anodizing > Bath size (inner size): width 50〇111111 parent 7 50〇11111 ^ 5 50111111 (approximately 168 liters) vibration mixer vibration motor: 250Wx 200VX 3 phases 1 unit (commodity Name Yuras vibrator: manufactured by Murakami Seiki Co., Ltd. and sold by Yaskawa Commercial Co., Ltd.) Vibration blade: effective area 300 × 150mm, thickness 0.6mm, 6 pieces, α = 15 ° (only the lower section is downward, and the rest are upward) Vibration Blade Amplitude: 1.5mm Vibration Frequency: 37Hz (adjusted via DC / AC converter) Inflator uses 3 ceramic diffuser tubes with an outer diameter of 75mm, an inner diameter of 50mm, a length of 450mrn, and an air aperture of about 200mm. . Rotary air pumps with a porosity of 40 / 〇, an air blow-out volume of about 120 liters / min, and a wheel output power of 150 W were used. The shaking device is given 20 times / min via a motor with a reducer or a drum motor. The paper size applies the Chinese National Standard (CNS) A4 specification (21〇X 297 mm) '-27 311303 ------- ------------- Order --------- W & WI Γ% Please read the notes on the back before filling out this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs

商品名新冷襯塾SA3-2 1.5KW 高) 555890 A7 —B7 五、發明說明(28 ) 後40mm寬之搖動。 設置附有搖動裝置之振動裝置 將振動馬達(砸)14固定在搖動用支承框2之適當部 位’經由直流交流變換器使振動馬達14以3〇Hz、振幅 〇 8mm振動。 陽極氧化浴(容量約15〇公升、液高4〇〇mm)之組成與 陽極氧化條件 硫酸 :200公克/公升 链含量:約4公克/公升 處理條件:如表1所示 冷卻用熱交換機 昭和鉛鐵(股)公司製造 能力· 4010千卡/小時 使用循環泵Trade name new cold lining SA3-2 1.5KW high) 555890 A7 —B7 V. Description of the invention (28) 40mm wide after shaking. A vibration device with a shaking device is provided. The vibration motor 14 is fixed to a proper position of the supporting frame 2 for swinging. The vibration motor 14 is vibrated at 30 Hz and an amplitude of 0.8 mm via a DC / AC converter. Composition of anodizing bath (capacity about 150 liters, liquid height of 400mm) and anodizing conditions Sulfuric acid: 200 g / litre Chain content: about 4 g / litre Processing conditions: As shown in Table 1, the cooling heat exchanger Showa Lead iron (stock) company manufacturing capacity · 4010 kcal / hour using circulating pump

最大流量120公升/分、265W、1.27A 脫脂浴(浴之内部尺寸:500x 75〇X 550mm、寬X表X 煙類脫脂劑:使用德克能霖S800(環烷類石油溶劑) 浴溫及時間:40°C、5分鐘 触刻浴(浴之内部尺寸·· 500χ 750χ 550) 硫酸(s.g.1.84) 500毫升/公升 磷酸(s.g.1.74) 1〇〇毫升/公升 鉻酸酐 30公克/公升 浴溫及時間 65°C、10分鐘 -----------------^9— (請先閲讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 28 311303 555890 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(29 ) 去污浴 硝酸 5%水溶液 封孔浴 浸潰於離子交換水之沸騰液 實施例7-2 除了被處理物之振動裝置(C)及搖動裝置(D)不動作之 外依照實施例7-1反覆操作。該結果如表6所示。 [表6] 外觀 耐氣候性*9 染色性*4 耐鹽水 噴霧% 實施例7-1 佳 500小時 均一性佳 140小時 實施例7-2 佳 300小時 均一性佳 96小時 *9耐氣候性··根據(老化試驗器)jis-K 5400 實施例8-1 如第4至6圖所示,使用具備振動攪拌裝置(A)、充氣 裝置(B)、被處理物振動裝置(C)及搖動裝置(D)之處理裝 置。Maximum flow rate 120 liters / minute, 265W, 1.27A degreasing bath (inside dimensions of the bath: 500x 75〇X 550mm, width X table X Tobacco degreasing agent: Use Deknin S800 (naphthenic petroleum solvent) bath temperature and Time: 40 ° C, 5 minutes touch etch bath (internal dimensions of the bath ·· 500χ 750χ 550) Sulfuric acid (sg1.84) 500ml / litre phosphoric acid (sg1.74) 100ml / litre chromic anhydride 30g / litre bath temperature And time 65 ° C, 10 minutes ----------------- ^ 9— (Please read the precautions on the back before filling this page) This paper size applies Chinese National Standard (CNS ) A4 size (210 X 297 mm) 28 311303 555890 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (29) Decontamination bath 5% nitric acid solution sealing bath immersed in the boiling of ion exchange water Liquid Example 7-2 Repeated operation was performed in accordance with Example 7-1 except that the vibration device (C) and shaking device (D) of the object to be processed did not operate. The results are shown in Table 6. [Table 6] Appearance weather resistance Property * 9 Dyeing property * 4 Salt spray resistance% Example 7-1 Good 500 hours Uniformity Good 140 hours Example 7-2 Good 300 Small Excellent uniformity 96 hours * 9 Weather resistance ·· According to (aging tester) jis-K 5400 Example 8-1 As shown in Figures 4 to 6, use a vibration stirring device (A) and an aeration device (B) The processing device of the vibration device (C) and the shaking device (D) of the processed object.

陽極氧化處理浴:500mmx 1250mmx 750mm(寬X長X 尚) 陽極氧化浴:約340公升 陽極氧化浴組成:硫酸200公克/公升、銘4公克/公 升 陰極板:銘板將(500mmx 60mmx 20mm)10塊豎排使 用 陽極板:使用500mmx 200mmx 10mm之鋁作為被處 -------------------訂—-----^9. (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(21〇 X 297公釐) 29 311303 555890 經濟部智慧財產局員工消費合作社印製 A7 五、發明說明(30) 理體 陰極板與陽極板之位置關係: 陽極安裝於處理浴之中央,處理浴兩側離開陽極 100mm之位置分別安裝5支陰極(參照第15圖)。以陽極 上部在液面下面70mm,下部在浴底上面7〇111111安裝。之 振動攪拌裝置(A): 振動馬達:400Wx 200Vx 3相2台(商品名悠拉斯 動器) 振動葉片·有效面積300χ 150mm、厚〇 6mm 6片、 安裝角度15° 振動葉片之振幅:1.5mm 振動頻率:37Hz(經由直流交流變換器控制) 充氣裝置: 使用外徑為75mm、内徑為50mm、長為8〇〇mm、氣 孔徑為約200私m之陶瓷製散氣管3支。每支之氣孔率為 40%、空氣吹出量約200公升/分。 用以使被處理物振動之振動裝置(c) ·· 將振動馬達(40 W) 14固定在搖動用支承框2之適當部 位,經由直流交流變換器使振動馬達14以3〇Hz、振幅 0.8mm振動。 搖動装置(D): 經由帶減速器電動機或筒式電動機以2〇次/分給予前 後40mm寬之搖動。 冷卻用熱交換器: _尺度適用中國^標準(CNS)A4規格⑽x 297公髮) 311303 --------訂---------^9— C請先閱讀背面之>i意事項再填寫本頁〕 555890 A7 B7 五、發明說明(31 ) 冷襯塾自動直冷式急速冷卻裝置 4010千卡/小時、電動機1.5 kw、口徑2 5 A 熱交換器用循環泵: 磁鐵泵 最大流量120公升/分、Max Head 8.6m、200V 輸出 265W、1·27Α、 整流器:Anodizing bath: 500mmx 1250mmx 750mm (width x length x still) Anodizing bath: about 340 liters Anodizing bath composition: 200 g / L of sulfuric acid, 4 g / L of cathode plate: 10 pieces of name plate (500mmx 60mmx 20mm) Use anode plate for vertical row: use 500mmx 200mmx 10mm aluminum as the quilt ------------------- Order --------- ^ 9. (Please read the Note: Please fill in this page again.) This paper size is in accordance with Chinese National Standard (CNS) A4 specification (21 × 297 mm) 29 311303 555890 Printed by A7 of the Consumers ’Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of invention (30) Position relationship between the cathode plate and the anode plate: The anode is installed in the center of the processing bath, and five cathodes are installed at positions 100 mm away from the anode on both sides of the processing bath (refer to FIG. 15). The upper part of the anode is 70 mm below the liquid surface, and the lower part is installed on the bottom of the bath 7011111. Vibration stirring device (A): Vibration motor: 400Wx 200Vx 3 phases and 2 units (brand name Ulas actuator) Vibrating blade · Effective area 300 × 150mm, thickness 6 mm, installation angle 15 ° Vibration blade amplitude: 1.5 mm Vibration frequency: 37Hz (Controlled by DC-AC converter) Inflator: 3 ceramic diffuser tubes with an outer diameter of 75mm, an inner diameter of 50mm, a length of 800mm, and an air hole diameter of about 200 μm. Each unit has a porosity of 40% and an air blowout volume of about 200 liters / minute. Vibration device (c) for vibrating the object to be processed. The vibration motor (40 W) 14 is fixed at an appropriate position of the support frame 2 for swinging, and the vibration motor 14 is passed through a DC / AC converter at 30 Hz and an amplitude of 0.8. mm vibration. Swing device (D): Gives a 40mm wide front and rear shake by a speed reducer motor or a barrel motor at 20 times / minute. Cooling heat exchanger: _Dimensions are applicable to China ^ standard (CNS) A4 specifications ⑽ x 297 public hair) 311303 -------- Order --------- ^ 9— CPlease read the first > I will fill in this page again if necessary] 555890 A7 B7 V. Description of the invention (31) Automatic lining of the cold lining: 4010 kcal / hour, 1.5 kw of motor, 2 5 A circulating pump for heat exchanger: Magnet pump maximum flow 120 liters / minute, Max Head 8.6m, 200V output 265W, 1.27A, rectifier:

Hi-Hi 直流電源裝置 60 V、100 A、6. Okw 交流輸入、200V、21.2A、7.35KVA 工序:依表1配置 又,本實施例之裝置亦設置有脫脂浴及封孔處理浴。 該結果如表7所示。Hi-Hi DC power supply device 60 V, 100 A, 6. Okw AC input, 200 V, 21.2 A, 7.35 KVA Process: configured according to Table 1 In addition, the device of this embodiment is also provided with a degreasing bath and a sealing bath. The results are shown in Table 7.

實施例U 除了實施例8-1中(C)及(D)不動作之外,依照實施例 8-1反覆操作。該結果如表7所示。 %-* --------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 外觀 耐氣候性*9 染色性*4 耐鹽水 喷霧*6 貫施例8_1 佳 500小時 均一性佳 140小時 實施例8-2 佳 300小時 均一性佳 96小時 實施你 使用與實施例84相同之裝置。使用鋁(A5〇52板)(尺 寸5〇〇x 2〇〇x 10mm)作為被處理體,陽極氧化條件為使用 實施例8之硫酸浴,在處理溫度為7t:、電流密度為i5A/d Πί下進行陽極氧化1〇分鐘Example U Except that (C) and (D) are inoperative in Example 8-1, the operation is repeated in accordance with Example 8-1. The results are shown in Table 7. %-* -------------------- Order --------- (Please read the notes on the back before filling this page) Intellectual Property of the Ministry of Economic Affairs Printed by the Consumer Cooperative of the Bureau. Weather resistance * 9 Dyeability * 4 Resistance to salt water spray * 6 Implementation Example 8_1 Good 500 hours uniformity 140 Good examples 8-2 Excellent 300 hours Uniformity 96 hours Implement your use The same device as in Example 84 was used. Aluminum (A5052 plate) (size 5000x200mm 10mm) was used as the object to be treated, and the anodizing conditions were the sulfuric acid bath of Example 8 at a processing temperature of 7t: and a current density of i5A / d. Anodizing for 10 minutes

311303 555890 五、發明說明(32 將實施例9-1所獲得之鋁板如第18圖所示區分,測定 各各中央部分之氧化膜厚度(// m)及硬度。 該結果如表8所示。[表8] 膜厚度311303 555890 V. Description of the invention (32 The aluminum plate obtained in Example 9-1 is divided as shown in FIG. 18, and the thickness (// m) and hardness of the oxide film in each central part are measured. The results are shown in Table 8. [Table 8] Film thickness

44.7 44.7 44.5 j5.2 — 44.9 平均膜厚 44.7 最小臈厚 44.1 最大膜厚 45 2 [表9] 44.1 44.4 44.5 44.9 44.9 44.7 519 509 520 527 511 519 514 521 526 516 512 512 516 520 512 518.0 511.0 527.0 最小硬度 最大硬度 --------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 實施例9-2 除了實施例9-1中只有振動流動攪拌裝置及充氣裝置 動作之外,依照實施例9-1反覆操作。所獲得之鋁表面之 氧化膜厚度及硬度分別如下所述。 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 32 311303 55589044.7 44.7 44.5 j5.2 — 44.9 Average film thickness 44.7 Minimum thickness 44.1 Maximum film thickness 45 2 [Table 9] 44.1 44.4 44.5 44.9 44.9 44.7 519 509 520 527 511 519 514 521 521 526 516 512 512 516 520 512 518.0 511.0 527.0 Minimum Hardness Maximum Hardness -------------------- Order --------- (Please read the precautions on the back before filling this page) Intellectual Property of the Ministry of Economic Affairs Bureau employee consumer cooperative printed Example 9-2 Except that only the vibrating flow stirring device and the inflatable device acted in Example 9-1, the operation was repeated in accordance with Example 9-1. The thickness and hardness of the obtained oxide film on the aluminum surface are described below. This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) 32 311303 555890

發明說明(Invention Description (

[表 11] 硬 度(HV) 405 400 411 401 397 401 398 406 410 400 410 401 415 402 402 卞Θ峴度 404.0 經濟部智慧財產局員工消費合作社印製 最小硬度 397.0 最大硬度 415.0 從比對表8至11可知,與本發明申請專利範圍第ι 項上述(Α)及(Β)裝置動作之實施例9_2比較,本發明申請 專利範圍第4項上述(A)、(Β)、(C)、(D)4個裝置均動作 之實施例9-1即使在同一溫度進行相同時間之陽極氧化, 可獲得膜厚度為10分之2厚、更均一,又,維氏硬度為約 10分之3之高數值,明瞭申請專利範圍第4項之優越性。 實施例10 為實施例1之(A)及(B)併用型之大型化案例。 (1)陽極氧化浴:耐熱性氣化乙烯類樹脂製(寬7〇〇m、 長 1000m、高 700mm)____ 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公髮) 33 311303 --------訂--------- (請先閱讀背面之注意事項再填寫本頁) 555890 A7[Table 11] Hardness (HV) 405 400 411 401 397 401 398 406 410 400 410 401 415 402 402 卞 Θ Dendity 404.0 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economics The minimum hardness 397.0 The maximum hardness 415.0 From comparison table 8 to 11 It can be seen that compared with the embodiment 9_2 of the above-mentioned (A) and (B) device operation of the scope of the present invention patent application, the above-mentioned (A), (B), (C), ( D) In Example 9-1 in which all four devices are operated, even if the anodization is performed at the same temperature and the same time, a film thickness of 2 / 10ths is more uniform, and the Vickers hardness is about 3 / 10ths. The high value indicates the superiority of the fourth item in the scope of patent application. Example 10 is a large-scale example of the combination of (A) and (B) of Example 1. (1) Anodizing bath: made of heat-resistant gasified vinyl resin (700m in width, 1000m in length, 700mm in height) ____ This paper size is applicable to China National Standard (CNS) A4 (210 X 297) 33 311303 -------- Order --------- (Please read the notes on the back before filling this page) 555890 A7

五、發明說明(34 ) (2)振動攪拌機:第1至2圖所示之構造 經濟部智慧財產局員工消費合作社印製 日本德克能(股)公司製造、超振動α _攪拌機α _5型、 振動馬達為悠拉斯振動器ΚΕΕ 10_2Β型750W 1台、附直 流交流變換器(1KW) 振動葉片:有效面積300x 150mm厚〇.6mm 6片、α =15。(只有下面之一段向下,其餘,向上) 振動葉片之振幅:1.5mm (3) 散氣管·日本德克能(股)公司製造之微充氣器 (BM-100) 3支散氣管之間隔(内徑50mm、外徑75〇mm、長 700mm)每支之空氣透過量12〇〇公升/分、氣孔率33至 38%、氣孔徑50至60// m 容積比重:2·2至2·5(每支) (4) 散氣管吹氣:旋轉式氣泵、輪出功率i5〇w、空氣 喷出量120公升/分 (5) 陽極氧化浴··收容液量420公升、硫酸2〇〇公克/ 公升、鋁4公克/公升 (6) 陰極板:鋁板1〇片 (7) 試驗體··與被處理相當之銘鑄造汽車部分(多數凹 凸) 大小'250mmx 750mmx 500mm (8) 冷卻用熱交換器:冷襯塾自動直冷式急速冷卻裝置 4010千卡/小時、電動機1.5kw、口徑25A(昭和鉛鐵(股 公司製造) (9) 熱交換器用循環泵:磁鐵泵 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 311303 --------訂--------- (請先閲讀背面之注意事項再填寫本頁) 34 555890 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(35 ) 最大流量120公升/分、Max Head 8.6m、200V輸出 265W、1·27Α、(伊瓦契 MD-100 RM) (10) 整流器:Hi-MiN直流電源裝置 額定值 60V-100A、6.0kw、交流輸入 200V、21.2A、 7.34KTA、中央製作所(股)公司 MB7C-600-01 (11) 極間距離:100mm (12) <處理浴之配置> 脫脂浴—水洗浴—蝕刻浴—水洗浴—去污浴—水洗浴 —陽極氧化浴—水洗浴—封孔處理浴—乾燥浴 (註)蝕刻浴:苛性鹼50公克/公升、RT 5分 去污浴:硝酸5%、RT 1分 封孔處理浴:離子交換過之水之沸騰水30分 電流密度:5A/d m2 陽極氧化在浴溫為30°C、總空氣排出量為120公升/ 分、振動流動攪拌之Hz數為40Hz、處理時間為8分鐘之 條件下可獲得平均膜厚20/zm之均一陽極氧化膜。不使用 振動流動攪拌裝置(A)時會產生燒焦,不能獲得良好之陽極 氧化膜,且電壓會從200V上昇至250V。 實施例11 使用與實施例1 〇同型之裝置,但變更下列項目。 (1) 陽極氧化浴:7〇〇mmx lOOOmmx 700mm(高) (2) 試驗體:lOOmmx 500mmx 300mm(高) (3) 散氣管:曰本德克能(股)公司之BM-100、氣孔率 33至3 8%、氣孔徑50至60// m、空氣排出量120公升/分、 -------------------訂---------^^^1 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 35 311303 555890 經濟部智慧財產局員工消費合作社印製 B7 五、發明說明(36 ) 5〇m_ (内徑)7〇m(外獲)、長則mm3支、散氣管間隔 120mm 在陽極氧化處理浴溫為3〇°C、總空氣排出量為12〇公 升/分下實施時需5分鐘’可獲得膜厚為15心,凹部之 任何-個部位膜厚都均一之陽極氧化膜。不使用振動流動 攪拌裝置(A)時,空氣噴出量若在6〇公升/分以上,則由於 陽極氧化膜變成不均一,空氣喷出量不能再增加且有燒焦 發生,電流密度亦不能上昇。 [效果] (1) 根據本發明與以往方法相比較,不會發生燒焦且可 實現3至5倍之高速化處理,可大幅度縮短陽極氧化之處 理時間,因此同時亦可達到節省能源化。又,若採用申請 專利範圍第5至第7項之系統,更可縮短全體之處理時 間。 (2) 根據本發明可大幅度提高陽極氧化膜之維氏硬 度0 (3) 根據本發明可獲得均一性高之陽極氧化膜,所以本 發明有利於製造感光轉筒(OPC轉筒)等。 (4) 因此,只要獲得與以往同程度品質之氧化臈,有陽 極氧化處理洛之溫度可比以往方法高5至10 °C之優點,冷 卻機之能力亦較小,較理想。具體而言,形成硬質氧化膜 時,以往方法為-5°C至5°C而本發明為10至15°C,較理想, 又,形成一般氧化膜時,以往方法為20°C左右,本發明則 為30至35°C,較理想。 ------------· I------訂--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 36 311303 555890 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 A7 B7 五、發明說明(37 ) (5) 即使有多數凹凸之物品或有10mni以下小孔(貫穿 孔或盲孔)之物品,連該凹部或小孔之内部都可充分陽極氧 化,凹部或小孔内亦可形成均一之氧化膜。因此,有利於 有凹凸之金屬板之陽極氧化處理、引擎關連零件、熱交換 器等具有複雜形狀物品之陽極氧化處理。 (6) 根據本發明所獲得之氧化膜比根據以往方法在同 一處理溫度所獲得之氧化臈較具光澤且硬度大,因此具有 耐摩損性、防腐蝕性、耐氣候性且氧化膜之均一性亦高。 (7) 充氣中空氣之噴出量由於若多於某一程度以上則 陽極氧化膜會變成不均一,因此喷出量有限制,但是,本 發明由於併用振動流動攪拌方法,至今空氣喷量之限度可 大幅度上昇,其結果浴之溫度可更下降,亦可提高電流密 度 (8) 根據本發明所獲得之氧化膜染色性佳。 [圖式之簡單說明] 第1圖為本發明申請專利範圍第丨項所使用裝置 具體例之側面圖。 第2圖為第1圖裝置之正面圖。 第3圖為第1圖裝置之上面圖。 第4圖為本發明申請專利範圍第4項所使用裝置之^ 具體例之側面圖。 第5圖為第4圖裝置之正面圖。 第6圖為第4圖裝置之上面圖。 第7圖為第5圖之X-X線斷面圖。 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 37 311303 --------------------訂--------- (請先閱讀背面之注意事項再填寫本頁} 555890 A7V. Description of the invention (34) (2) Vibration mixer: printed in Figure 1 to 2 by the Intellectual Property Bureau of the Ministry of Economic Affairs, Employees' Cooperatives, printed by Japan Dekenen Co., Ltd., super vibration α _ mixer α _5 type 1. Vibration motor is one ÖLAS vibrator KEE 10_2B type 750W, with DC AC converter (1KW) vibrating blade: effective area 300x 150mm thickness 0.6mm 6 pieces, α = 15. (Only the lower section is downward, the rest is upward.) Amplitude of the vibration blade: 1.5mm (3) Diffuser • Micro-inflator (BM-100) made by Japan Deknen Co., Ltd. The distance between the 3 diffuser tubes ( (Inner diameter: 50mm, outer diameter: 75mm, length: 700mm) Air permeation capacity is 12,000 liters / minute, porosity is 33 to 38%, and porosity is 50 to 60 // m. Volumetric specific gravity: 2 · 2 to 2 · 5 (each) (4) Blowing air pipe: Rotary air pump, i50w output power, 120 liters / min. (5) Anodizing bath ·· Containing liquid volume 420 liters, sulfuric acid 〇〇 Gram / liter, aluminum 4 gram / liter (6) Cathode plate: 10 pieces of aluminum plate (7) Test body · The equivalent of the processed part Cast automotive parts (most bumps) Size '250mmx 750mmx 500mm (8) Cooling heat Exchanger: Cold-lined automatic direct-cooling rapid cooling device 4010 kcal / hour, motor 1.5kw, caliber 25A (Showa Lead Iron Co., Ltd.) (9) Circulating pump for heat exchanger: magnet pump This paper is applicable to China National Standard (CNS) A4 Specification (210 X 297 mm) 311303 -------- Order --------- (Please read the precautions on the back first (Fill in this page again) 34 555890 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (35) Maximum flow 120 liters / minute, Max Head 8.6m, 200V output 265W, 1.27A, (Ivac) MD-100 RM) (10) Rectifier: Hi-MiN DC power supply device rated 60V-100A, 6.0kw, AC input 200V, 21.2A, 7.34KTA, Central Manufacturing Co., Ltd. MB7C-600-01 (11) Distance between electrodes: 100mm (12) < Configuration of treatment bath > Degreasing bath—water bath—etching bath—water bath—decontamination bath—water bath—anodic oxidation bath—water bath—sealing treatment bath—drying bath ( Note) Etching bath: caustic 50 g / litre, RT 5 minutes decontamination bath: 5% nitric acid, RT 1 minute sealing treatment bath: ion-exchanged boiling water 30 minutes, current density: 5A / d m2 A uniform anodized film with an average film thickness of 20 / zm can be obtained under the conditions of a bath temperature of 30 ° C, a total air discharge of 120 liters / minute, a vibration flow of 40 Hz, and a processing time of 8 minutes. Scorching occurs when vibrating the flow stirring device (A), and good anodic oxygen cannot be obtained Membrane, and the voltage will increase from 200V to 250V. Example 11 The same type of device as in Example 10 was used, but the following items were changed. (1) Anodizing bath: 700mmx 1000mmx 700mm (high) (2) Test body : LOOmmx 500mmx 300mm (height) (3) Diffuser: BM-100 of Japan Dekenen Co., Ltd., porosity 33 to 38%, porosity 50 to 60 // m, air discharge 120 liters / Points, ------------------- Order --------- ^^^ 1 (Please read the notes on the back before filling this page) This paper The scale is applicable to the Chinese National Standard (CNS) A4 specification (210 X 297 mm) 35 311303 555890 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs B7 V. Description of the invention (36) 50m_ (inner diameter) 70m (outside (Obtained), length of 3 mm, air diffuser interval of 120mm, it takes 5 minutes when the temperature of the anodizing bath is 30 ° C and the total air discharge is 120 liters / min. Anodized film with uniform film thickness at any part. When the vibration flow stirring device (A) is not used, if the air ejection amount is more than 60 liters / minute, because the anodized film becomes non-uniform, the air ejection amount cannot be increased further and scorch occurs, and the current density cannot be increased. . [Effects] (1) Compared with the conventional method, according to the present invention, scorching does not occur and a high-speed processing of 3 to 5 times can be realized, which can greatly reduce the processing time of anodization, so it can also save energy. . In addition, if the system in the scope of patent application Nos. 5 to 7 is adopted, the overall processing time can be further shortened. (2) According to the present invention, the Vickers hardness of the anodized film can be greatly improved. (3) According to the present invention, an anodized film with high uniformity can be obtained. Therefore, the present invention is advantageous for manufacturing a photosensitive drum (OPC drum) and the like. (4) Therefore, as long as osmium oxide with the same level of quality is obtained, the temperature of anode oxidation treatment Luo can be 5 to 10 ° C higher than the previous method, and the capacity of the cooler is also small, which is ideal. Specifically, when forming a hard oxide film, the conventional method is -5 ° C to 5 ° C and the present invention is 10 to 15 ° C, which is ideal. Moreover, when forming a general oxide film, the conventional method is about 20 ° C. In the present invention, it is preferably 30 to 35 ° C. ------------ · I ------ Order --------- (Please read the notes on the back before filling out this page) This paper size applies to Chinese national standards (CNS) A4 specification (210 X 297 mm) 36 311303 555890 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (37) (5) Even if there are most concavo-convex items or small holes below 10mni ( Through holes or blind holes), even the inside of the recess or small hole can be fully anodized, and a uniform oxide film can be formed in the recess or small hole. Therefore, it is advantageous for anodizing treatment of metal plates with unevenness, anodizing treatment of complicated parts such as engine related parts, heat exchangers. (6) The oxide film obtained according to the present invention is more lustrous and harder than the hafnium oxide obtained at the same processing temperature according to the conventional method, so it has abrasion resistance, corrosion resistance, weather resistance and uniformity of the oxide film. Also high. (7) If the amount of air sprayed during inflation is more than a certain level, the anodic oxide film will become non-uniform, so the amount of sprayed is limited. However, the present invention uses the vibration flow stirring method in combination, so far the limit of the amount of air sprayed It can be greatly increased, and as a result, the temperature of the bath can be further decreased, and the current density can also be increased (8) The dyeability of the oxide film obtained according to the present invention is good. [Brief description of the drawings] Fig. 1 is a side view of a specific example of a device used in item 丨 of the patent application scope of the present invention. Figure 2 is a front view of the device of Figure 1. Figure 3 is a top view of the device of Figure 1. FIG. 4 is a side view of a specific example of the device used in item 4 of the patent application scope of the present invention. Figure 5 is a front view of the device of Figure 4. Figure 6 is a top view of the device of Figure 4. Figure 7 is a sectional view taken along line X-X in Figure 5. This paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) 37 311303 -------------------- Order -------- -(Please read the notes on the back before filling out this page) 555890 A7

五、發明說明(38 ) 經濟部智慧財產局員工消費合作社印製 第8圖為第6圖之γ-γ線斷面圖。 第9圖為振動葉片固定在振動棒之一個態樣之擴大部 分之斷面圖 第1 〇圖為橫振動攪拌裝置之1例之平面圖。 第11圖為第10圖之斷面圖。 第12圖為本發明所使用裝置之其他具體例之平面 圖。 第13圖為第12圖裝置之正面圖。 第14圖為第12圖裝置之側面圖。 第15圖為陽極及陰極配置例之平面圖。 第16圖為實施例4與比較例4中陽極氧化浴之溫度與 所獲得氧化膜之維氏硬度之關係圖。 第17圖為本發明實施例所使用之系統之流程圖(A)至 (D)與申請專利範圍所使用之記號相對應。 第18圖為鋁板之區分方法及測定部位之圖。 第19圖為大型處理浴中散氣管之配置態樣圖。 第20圖對照陽極氧化軟起動之設定電流密度變化狀 態之圖。 第21圖實施例中所使用試驗板固定裝置之側面圖。 [符號之說明] 1 處理浴(亦可具有前處理浴或後處理浴) 2 搖動用支承框 3 用以使搖動用支承框搖動之搖動馬達 4 振動攪拌裝置之振動馬達 -------------------訂--------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 38 311303 555890 A7 五、發明說明(39 ) 5 7 9 10 11 13 14 16 18 20 22 24 26 28 30 32 33 陽極 6 滑動式電極支承件 8 裝置托架 送至散氣管之壓縮空氣入口 電熱器 η 陰極棒支承件 使搖動用支承框振動之振動 振動棒 振動葉片固定構件 彈簧 下部支撐框 螺絲 平衡器 電熱器 陰極匯流條支承件 從陽極6垂吊連接之連接部 试驗板 34 陰極 搖動框用粍架 17 19 21 23 25 27 29 31 散氣管 馬達 振動葉片 振動應力分散機構 上部支撐框 氟素類聚合臈 振動傳達框 附螺絲之支持棒 充氣用空氣壓縮機 陽極 鋁線 丁 I ϋ ϋ ϋ ϋ ί mmte i·— ϋ · ϋ in 1 J 、 I ϋ (請先閱讀背面之注意事項再填寫本頁) S-. 經濟部智慧財產局員工消費合作社印製 本紐尺度適用中關家標準(CNS)A4規格(210 X 297公楚· 311303V. Description of the invention (38) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs Figure 8 is a γ-γ cross-sectional view of Figure 6. Fig. 9 is a sectional view of an enlarged portion of a state where the vibration blade is fixed to the vibrating rod. Fig. 10 is a plan view of an example of a horizontal vibration stirring device. Figure 11 is a sectional view of Figure 10. Fig. 12 is a plan view of another specific example of the device used in the present invention. Figure 13 is a front view of the device of Figure 12. Fig. 14 is a side view of the device of Fig. 12; Fig. 15 is a plan view of an anode and cathode arrangement example. Fig. 16 is a graph showing the relationship between the temperature of the anodizing bath in Example 4 and Comparative Example 4 and the Vickers hardness of the obtained oxide film. Fig. 17 is a flowchart (A) to (D) of the system used in the embodiment of the present invention corresponding to the symbols used in the scope of patent application. Fig. 18 is a method of distinguishing an aluminum plate and a measurement portion. Fig. 19 is a configuration diagram of the air diffuser in a large-scale treatment bath. Fig. 20 is a graph comparing the change of the set current density of the anodizing soft start. Fig. 21 is a side view of the test plate fixing device used in the embodiment. [Explanation of symbols] 1 treatment bath (possibly with pre-treatment bath or post-treatment bath) 2 support frame for shaking 3 swing motor for shaking support frame for swing 4 vibration motor of vibration stirring device ------ ------------- Order --------- (Please read the precautions on the back before filling this page) This paper size is applicable to China National Standard (CNS) A4 specification (210 X 297 mm) 38 311303 555890 A7 V. Description of the invention (39) 5 7 9 10 11 13 14 16 18 20 22 24 26 28 30 32 33 Anode 6 Sliding electrode support 8 Device bracket sent to the air tube for compression Air inlet heater η Cathode rod support Vibration of shaking support frame Vibration rod vibration blade fixing member Spring lower support frame Screw balancer Electric heater cathode bus bar support Connection portion test plate 34 hanging from anode 6 17 19 21 23 25 27 29 31 Cathode shaker frame 17 19 21 23 25 27 29 31 Dispersion tube motor vibration blade Vibration stress dispersing mechanism Upper support frame Fluoropolymer polymer 臈 Vibration transmission frame Support screw with screw Air compressor anode aluminum wire D I ϋ ϋ ϋ ϋ ί mmte i · — · Ϋ in 1 J, I ϋ (Please read the notes on the back before filling out this page) S-. Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs, this standard applies to the Zhongguanjia Standard (CNS) A4 Specification (210 X 297 Gongchu311311

Claims (1)

申請專利範圍 2. 555890 一種金屬陽極氧化處理系、统,其特徵為:於金屬陽極氧 化工序中,使 (A) 设有··包含振動馬達之振動產生機構,·與振動 產生機構連動而使一段或多段固定於在攪拌槽内振動 之振動捧上之振動葉片,以振幅為05s3〇mm、振動 數為200至800次/分產生振動流動之振動流動攪拌機 構,用以控制振動馬達使之可在1〇至5〇〇1^之間任意 振動之直流交流變換器;及設於振動產生機構與上述振 動流動攪拌機構的連接部之振動應力分散機構之對處 理浴的振動流動攪拌裝置、以及 (B) 作為對處理浴之充氣裝置之使用氣孔徑為ι〇 至400从m、氣孔率為30至4〇%之陶瓷製散氣管之充氣 裝置同時動作。 一種金屬陽極氧化處理系統,其特徵為:於金屬陽極氧 化工序中,使 (A) 設有:包含振動馬達之振動產生機構;與振動 產生機構連動而使一段或多段固定於在攪拌槽内振動 之振動捧上之振動葉片,以振幅為〇5至3 〇mm、振動 數為200至800次/分產生振動流動之振動流動攪拌機 構;用以控制振動馬達使之可在1 〇至5〇〇Hz之間任魚 振動之直流交流變換器;及設在振動產生機構與上述振 動流動攪拌機構的連接部之振動應力分散機構之對處 理浴的振動流動攪拌裝置、 (B) 作為對處理浴之充氣裝置之使用氣孔徑為 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) I --------t---------線 (請先閱讀背面之注意事項再填寫本頁) 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 555890 六、申請專利範圍 至400 v m、氣孔率為30至40%之陶瓷製散氣管之充氣 裝置、以及 (C)用以透過垂吊著被處理物之電極棒,使用經由 直流交流變換器調節為10至60Hz之振動馬達,給予被 處理物振幅為0.5至1.0mm、振動數1〇〇至3〇〇次/分之 振動之振動裝置同時動作。 3· —種金屬陽極氧化處理系統,其特徵為:於金屬陽極氧 化工序中,使 訂 線 (A) 设有·包含振動馬達之振動產生機構;與振動 產生機構連動而使一段或多段固定於在攪拌槽内振動 之振動捧上之振動葉片,以振幅為〇 5至3 〇mm、振動 數為200至800次/分產生振動流動之振動流動攪拌機 構;用以控制振動馬達使之可在10至5〇〇1^之間任意 振動之直流交流變換器;及設在振動產生機構與上述振 動流動攪拌機構的連接部之振動應力分散機構之對處 理浴的振動流動攪拌裝置、 (B) 作為對處理浴之充氣裝置之使用氣孔徑為 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 至400 /zm、氣孔率為30至40%之陶瓷製散氣管之充氣 裝置、以及 (C) 用以透過垂吊著被處理物之電極棒,給予被處 理物搖動幅為10至100mm、搖動數為10至3〇次/分之 搖動之搖動裝置同時動作。 4. 一種金屬陽極氧化處理系統,其特徵為:於金屬陽極氧 化工序中,使 本紙張尺度適財關家標準(CNS)A4規格⑵Q χ视公爱) 41 311303 555890 經濟部智慧財產局員工消費合作社印製 A8 B8 C8 D8 -- ~ --—— 六、申請專利範圍 (A) 設有:包含振動馬達之振動產生機構;與振動 產生機構連動而使一段或多段固定於在攪拌槽内振動 之振動捧上之振動葉片,以振幅為〇5至3 〇mm、振動 數為200至800次/分產生振動流動之振動流動攪拌機 構,用以控制振動馬達使之可在1〇至5〇〇Hz之間任意 振動之直流交流變換器;及設於振動產生機構與上述振 動流動攪拌機構的連接部之振動應力分散機構之對處 理浴之振動流動攪拌裝置、 (B) 作為對處理浴之充氣裝置之使用氣孔徑為 至400 //m、氣孔率為30至4〇%之陶瓷製散氣管之充氣 裝置、 (C) 用以透過垂吊著被處理物之電極棒,使用經由 直流交流變換器調節為1 〇至60Hz之振動馬達,給予被 處理物振幅為〇·5至1 .Omm、振動數1〇〇至3〇〇次/分之 振動之振動裝置、以及 (D) 用以透過垂吊著被處理物之電極棒,給予被處 理物搖動幅為10至l〇〇mm、搖動數為10至30次/分之 搖動之搖動裝置同時動作。 5· 一種金屬陽極氧化處理系統,其特徵為:在金屬陽極 氧化工序加上在其前處理工序及/或後處理工序之至少 一個工序中,只使上述(A)之裝置動作、使上述(A)、(W 之裝置同時動作、使上述(A)、(B)及(C)之裝置同時動 作、使上述(A)、 (B)及(D)之裝置同時動作或是使上述 (A)、(B)、(C)及(D)之裝置同時動作。 11 --------訂---------線 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 42 311303 555890Patent application range 2. 555890 A metal anodizing treatment system and system, characterized in that: (A) is provided with a vibration generating mechanism including a vibration motor in the metal anodizing process, and is linked with the vibration generating mechanism so that One or more sections are fixed on the vibration blades vibrating in the mixing tank, and the vibration flow stirring mechanism that generates vibration flow with an amplitude of 05s30mm and a vibration number of 200 to 800 times / minute is used to control the vibration motor to make it A DC-AC converter capable of arbitrarily vibrating between 10 and 5000; and a vibration flow stirring device for a processing bath, a vibration stress dispersing mechanism provided at a connection portion between the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism, And (B) As an inflation device for the treatment bath, an inflation device using a ceramic diffuser with a pore size of ˜400 to m and a porosity of 30 to 40% operates simultaneously. A metal anodizing treatment system, characterized in that in the metal anodizing process, (A) is provided with: a vibration generating mechanism including a vibration motor; and one or more sections are fixed to be vibrated in a stirring tank in conjunction with the vibration generating mechanism. The vibration blade on the vibrating arm is a vibration flow stirring mechanism that generates vibration flow with an amplitude of 05 to 30 mm and a number of vibrations of 200 to 800 times / minute; it is used to control the vibration motor so that it can reach 10 to 50. DC-to-AC converter for any fish vibration between 0 Hz; and a vibration flow stirring device for a processing bath provided in a vibration stress dispersing mechanism provided at a connection portion between the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism, (B) as a processing bath The air hole used by the inflatable device is based on the paper size and applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) I -------- t --------- line (please first (Please read the notes on the back and fill in this page again.) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. 555890 6. Inflatable device made of ceramic diffuser with a patent scope of 400 vm and a porosity of 30 to 40%. (C) A vibrating motor that is adjusted to 10 to 60 Hz through a DC / AC converter through an electrode rod that hangs the object to be processed, and the object to be processed has an amplitude of 0.5 to 1.0 mm and a vibration number of 100 to 3 The vibration device which vibrates at 00 times / minute operates simultaneously. 3. A metal anodizing treatment system, characterized in that in the metal anodizing process, the thread (A) is provided with a vibration generating mechanism including a vibration motor; and one or more sections are fixed in linkage with the vibration generating mechanism. The vibration blade that is vibrating in the stirring tank is a vibration flow stirring mechanism that generates vibration flow with an amplitude of 05 to 30 mm and a number of vibrations of 200 to 800 times / minute; it is used to control the vibration motor so that A DC-AC converter with arbitrary vibration between 10 and 5000; and a vibration flow stirring device for a treatment bath, a vibration stress dispersing mechanism provided at a connection portion between the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism, (B) As an inflatable device for the treatment bath, the aeration device is a ceramic air diffuser printed to 400 / zm and a porosity of 30 to 40% by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, and (C) for transmitting The electrode rod of the object to be processed is hung, and the object to be processed is shaken with a shaking range of 10 to 100 mm and a shaking number of 10 to 30 times per minute. 4. A metal anodizing treatment system, characterized in that during the metal anodizing process, the paper size is adapted to the financial standards (CNS) A4 specification ⑵Q χ as public love) 41 311303 555890 Intellectual Property Bureau staff of the Ministry of Economic Affairs employee consumption Printed by the cooperative A8 B8 C8 D8-~ ------ 6. Scope of patent application (A) Provided: Vibration generating mechanism including vibration motor; Linked with the vibration generating mechanism to fix one or more sections to vibration in the mixing tank The vibrating blade on the vibrating arm is a vibration flow stirring mechanism that generates vibration flow with an amplitude of 05 to 30 mm and a number of vibrations of 200 to 800 times / minute. It is used to control the vibration motor so that it can reach 10 to 50. DC-AC converter with arbitrary vibration between 0Hz; and vibration flow stirring device for the processing bath provided at the vibration stress dispersing mechanism of the connection part of the vibration generating mechanism and the above-mentioned vibration flow stirring mechanism, (B) as the processing bath Inflator using ceramic diffuser with a pore diameter of up to 400 // m and a porosity of 30 to 40%, (C) Electrode rod for hanging the object to be treated A vibration motor adjusted to a frequency of 10 to 60 Hz by a DC / AC converter is used to provide a vibration device having a vibration amplitude of 0.5 to 1.0 mm and a vibration number of 100 to 3,000 times per minute, and ( D) The swinging device for suspending the object to be processed through the electrode rod to give the object to be shaken with a swing width of 10 to 100 mm and a shaking number of 10 to 30 times per minute simultaneously operates. 5. A metal anodizing treatment system, characterized in that in at least one of the metal anodizing step plus the pre-processing step and / or the post-processing step, only the device of (A) is operated, and the above-mentioned ( A), (W devices operate simultaneously, the devices (A), (B), and (C) operate simultaneously, the devices (A), (B), and (D) operate simultaneously or the above ( The devices of A), (B), (C) and (D) operate simultaneously. 11 -------- Order --------- line (please read the precautions on the back before filling in this Page) This paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) 42 311303 555890 六、申請專利範圍 6·如申請專利範圍第5項之金屬陽極氧化處理系統,其 中,上述前處理工序及後處理工序係脫脂工序、選自由 電解拋光及化學拋光所成之組群之拋光工序、熱水封孔 處理工序中之至少一個工序者。 7·如申請專利範圍第1至6項中任何一項之金屬陽極氧化 處理系統,其中,由金屬所成之被處理物為具有縫隙部 之最窄寬度或孔徑小於1 〇mm之凹陷或貫穿孔者。 ---------------------訂 ---------線 (請元閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 311303 436. Scope of patent application 6. The metal anodizing treatment system according to item 5 of the scope of patent application, wherein the above-mentioned pre-treatment process and post-treatment process are degreasing processes and polishing processes selected from the group consisting of electrolytic polishing and chemical polishing. Or at least one of the hot water sealing treatment processes. 7. The metal anodizing treatment system according to any one of claims 1 to 6, wherein the object to be processed made of metal is a depression or penetration having the narrowest width of the gap portion or a pore diameter of less than 10 mm Hole. --------------------- Order --------- line (please read the notes on the back and fill in this page) Intellectual Property Bureau of the Ministry of Economic Affairs The paper size printed by the employee consumer cooperative is applicable to the Chinese National Standard (CNS) A4 (210 X 297 mm) 311303 43
TW089105542A 1999-04-02 2000-03-27 A metallic anode oxidation treatment system utilizing a vibration flow agitation TW555890B (en)

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CN102839407A (en) * 2012-09-18 2012-12-26 无锡市喷特环保工程有限公司 Piston rapid aluminum oxidation single machine
CN114277403A (en) * 2021-12-22 2022-04-05 曹文浩 Chemical electrolytic tank
TWI802133B (en) * 2021-12-07 2023-05-11 日商荏原製作所股份有限公司 Plating method and plating device

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Cited By (4)

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Publication number Priority date Publication date Assignee Title
CN102839407A (en) * 2012-09-18 2012-12-26 无锡市喷特环保工程有限公司 Piston rapid aluminum oxidation single machine
TWI802133B (en) * 2021-12-07 2023-05-11 日商荏原製作所股份有限公司 Plating method and plating device
CN114277403A (en) * 2021-12-22 2022-04-05 曹文浩 Chemical electrolytic tank
CN114277403B (en) * 2021-12-22 2024-04-19 兰溪自立环保科技有限公司 Electrolytic tank for chemical industry

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