201134987 六、發明說明： 【發明所屬之技#?領域】 [0001] 本發明涉及電鍍技術頷域，尤A、* ώ a '、/乂及―種可節省窆朗 提高電鍍均勻度及電鍍效率之電鍍裴置 <間教 【先前技術】 [0002] 電鍍係指採用電解裝置，利用窗& B 〇 則錢•反應原理將^ 陽極金屬之鹽鼐电鍍液中之陽極八 I括 質，金屬單質沈積於待電鍛工件離+ 屬單 电锻工件表面形成鑛層之 面加工方法。所述電解|置包括與電源正極相種表 極、與電源負極相連通之陰極及用於盛裝電c 槽。通常，所述陽極為陽極金屬棒。所賴極^ 沒於電舰中’料生成陽極金屬離子，並補充t養 中之陽極金屬離子含量，從而維持電錢液中之t 離子濃度處於預定範圍内。 金屬 [0003] 電鍍工藝歧驗製作電路板，詳情可參見讀：A τ C〇bley，D.R. Gabe; for achieving.. high叩㈣c卿仏诚⑽rGplating PCB lndUSt-； ^-Uit World; 200 1, V〇lumethe ，ISSUe3，Page:19 _ 25。先前之-種電鍍裝w 包括電鍍槽、傳送單元、陽極板與導電刷。該傳送單元 與陽極板均位於電錄槽内。待锻電路板於傳送單元之帶 動下/σ 1線移動。陽極板垂直待鑛電路板之移動方向 «X置於相電路板之㈣，用於向待電鍍液巾提供陽離 子導電刷位於待链電路板之正上方，用於接觸待鑛電 路板並向待鑛電路板之上表面提供電流以進行電錢。由 099110241 表單編號Α0101201134987 VI. Description of the Invention: [Technology of Invention] Field [0001] The present invention relates to the field of electroplating technology, in particular, A, * ώ a ', / 乂 and "species can save the plating uniformity and electroplating efficiency Electroplating device <Intermediate teaching [Prior Art] [0002] Electroplating refers to the use of an electrolysis device, using the window & B 〇 钱 • 反应 反应 反应 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极 阳极The metal element is deposited on the surface of the workpiece to be electrically forged from the surface of the single electric forged workpiece to form a mineral layer. The electrolysis|suction includes a cathode which is in contact with the anode of the power source, a cathode which is in communication with the negative pole of the power source, and a tank for holding the electric c. Typically, the anode is an anode metal rod. The radiant ^ is not in the electric ship's material to generate anode metal ions, and to supplement the anode metal ion content in the t-culture, so as to maintain the t ion concentration in the liquid money liquid within a predetermined range. Metal [0003] Electroplating process for the production of circuit boards, see for reading: A τ C〇bley, DR Gabe; for achieving.. high叩 (four) c Qing Yu (10) rGplating PCB lndUSt-; ^-Uit World; 200 1, V 〇lumethe, ISSUe3, Page: 19 _ 25. The previous electroplating package w includes a plating bath, a transfer unit, an anode plate and a conductive brush. The transfer unit and the anode plate are both located in the electric recording groove. The circuit board to be forged is moved by the transmission unit / σ 1 line. The moving direction of the anode plate vertical to be mined circuit board «X is placed on the phase circuit board (4), and the cationic conductive brush for providing the liquid towel to be plated is located directly above the circuit board to be chained, for contacting the circuit board to be mined and waiting Electricity is supplied to the upper surface of the mining circuit board for electricity. By 099110241 Form number Α0101
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0992C 201134987 於待鑛電路板沿直線移動，㉞料Μ 提高電鑛效率，如此，電錢裝置需要佔據大量= ，陽極板之設置方式使得待鍍 ^ Μ * 心遠離陽極板處 之％離子d低’直接導致料電路板表k鍍 不均。而利用導電刷向待鍍電路板表面傳導電流：一； 面’接觸面積小’不利於提高電錢效率，另一:面導 電刷自身亦會沈積錢層，使用—段時間就得更換導電刷 〇 Ο [0004] 【發明内容】 有鑑於此，提供-種電麟置以節省韻並提高電鍵均 勻度及電鑛效率實屬必要。 [0005] 一種電鍍裝置，用於對連續傳送之柔性基材進行電鍍。 所述電鍍裝置包括一放送輪、一卷收輪、—盛有電鍍液 之電錄槽、複數可導電之傳送輪以及複數陽極板。所述 放送輪與卷收輪均設置於所述電f鑛槽外。所述複數傳送 輪與複數陽極板均設置於電鍍槽内。所述複數陽極板及 Ο 複數可導電之傳送_均浸沒於所述電鍍液中。所述放送 輪用於將柔性基材放送至電鍍槽内。所述複數傳送輪用 於藉由轉動將放送輪放送之柔性基材傳送至卷收輪，並 用於導電給所傳送之柔性基材。所述複數陽極板基本平 行設置。每一陽極板均具有相對之第一端與第二端，於 任意相鄰之兩個陽極板中，兩個陽極板之第一端相鄰， 兩個陽極板之第二端相鄰。一陽極板之第一端與一傳送 輪相鄰，另一陽極板之第二端與另一傳送輪相鄰。所述 柔性基材經過所述兩個傳送輪時於所述相鄰之兩個陽極 099110241 表單編號A0101 第5頁/共22頁 0992018035-0 201134987 板之間被傳送。所述複數陽極板用於作為陽極使得於複 數傳送輪之間傳送之柔性基材於導電狀況下進行電鍍。 所述卷收輪用於卷收來自複數傳送輪之電鍍後之柔性基 材。 [0006] [0007] [0008] [0009] 本技術方案之電鍍裝置之電鍍裝置具有複數傳送輪，所 述複數傳送輪除了向柔性基材提供電流，還可移動電鍍 中之柔性基材並改變柔性基材之移動方向，從而可使柔 性基材於電鑛槽内擔雄·如進，充分利用電鍵槽之空間， 提高電鍵效率。此外，所述複數陽極板均平行於柔性基 材’從而柔性基材表面各處電流密度均相等，可提高電 鑛之均勻性。 【實施方式】 以下將結合附圖與實施例對本技術方案之電.鑛裝置進行 詳細說明。 請參閱圖1，本技術方案提学m種電錄裝置^1〇，用於對連 續傳送之柔性基材進行電鑛。所述柔性基材為柔性材質 。所述電锻裝置10包括一放送輪11、_卷收輪12、一盛 有電鍍液之電鍍槽13、複數可導電之傳送輪、複數絕緣 之傳動輪、一可導電之傳動滾輪、複數陽極板、複數絕 緣隔板、-陽離子補充槽19與-陽離子自動補充系統2〇 。所述電鍍液可為包含硫酸銅、硫酸與鹽酸等之混合液 所述放送輪11與卷收輪12均位於所述電鍍槽13外。所述 放送輪η狀捲㈣性基材並向電储13喊送柔性基 099110241 材。所述卷收輪12用於卷收來自故送輪u 表單編號A0101 第6頁/共22頁 之、於電鍍槽 0992018035-0 201134987 13内電鍍後之基材。亦即，所述柔性基材可自所述放送 輪11進入電鍍槽13，並於完成電鍍後被輸出至所述卷收 輪12並被卷收輪12卷收。 [0010] 所述電鍍槽13可為一端不封口之長方形槽體，其包括相 連接之側壁130與底壁131。所述電鍍槽13具有相對之第 一側132與第二侧133。本實施例中，所述放送輪11與卷 收輪12分別靠近所述第一側132與第二側133。優選地， 所述電鍍槽13内靠近底壁131處可設置攪拌管134，所述 0 攪拌管134用於向電鍍槽13内喷出氣體以攪拌電鍍槽13内 之電鍍液。 [0011] 所述複數可導電之傳送輪均浸沒於所述電鍍液中。所述 複數可導電之傳送輪均用於藉由轉動將放送輪11放送之 柔性基材傳送至卷收輪12，並用於導電給傳送之柔性基 材。每一傳送輪均包括傳送軸與套設於所述傳送軸之滚 輪。所述複數傳送輪之傳送軸均可藉由齒輪或皮帶機械 诖：&於151 —鰓叙装f I»去示、，你而於所怵酿動g之帶 ^ ^ Wfc* V I ,·> I — * · / r 、 ▼ ▼ ， * · I - o 動下以相同之速度旋轉。每一滾輪均可於與之對應之傳 送軸之帶動下旋轉。所述滾輪採用不銹鋼製成，且其表 面鍍有金屬鈦以避免所述滚輪本身沈積鍍層。本實施例 中，所述複數傳送輪於所述電鍍槽13内沿電鍍槽13之深 度方向於第一側132與第二側133交替分佈。所述複數傳 送輪之數量為七個，分別為第一傳送輪140、第二傳送輪 141、第三傳送輪142、第四傳送輪143、第五傳送輪144 、第六傳送輪145與第七傳送輪146。所述第一傳送輪 140、第三傳送輪142、第五傳送輪144與第七傳送輪146 099110241 表單編號A0101 第7頁/共22頁 0992018035-0 201134987 平行設置於電鍍槽13内之第—側，且所述第—傳送輪⑷ 、第三傳送輪142、第五傳送輪144與第七傳送輪146之 中心均位於—條直線上。所述第二傳送輪141、第四傳送 輪143與第六傳送輪145均設置於電鑛槽13内之第二側 133。所述第二傳送輪141、第四傳送輪143與第六傳送 輪145之t心均位於-條直線上。所述第—傳送輪、 第三傳送輪142、第五傳送輪144與第七傳送輪146中， 沿所述電鍍槽13之深度方向上相鄰之兩個傳送輪中心之 間距為傳送輪直徑之兩倍。所述第二傳送輪141、第四傳 璆輪143與第六傳送輪145中，沿所述電鍍槽13之深度方 向上相鄰之兩個傳送輪中心之間距為傳送輪直徑之兩倍 。所述複數傳送輪之直徑相等，沿電鍍槽13之深度方向 上，相鄰之兩個傳送輪之中心轴線之間距恰等於所述傳 送輪之直徑。如，所述第二傳送輪141與所述第一傳送輪 140於電鍍槽13之軸線方向上之間距即等於所述傳送輪之 直徑。從而，於本實施例中，柔蠢基材於所述電鍍槽13 内之移動方向平行於底壁131所於之平扁。 [0012] 所述複數絕緣之傳動輪均位於所述電鍍槽13内。所述複 數傳送輪之結構與傳動輪之大致相同，且所述複數傳送 輪之傳輸線速度等於複數傳動輪之傳輸線速度。若所述 複數傳送輪與傳動輪共用一驅動器，則所述複數傳送輪 直徑與傳動輪之直徑應相同、所述複數傳動輪包括至少 第一傳動輪150與至少·一第二傳動輪151。所述至少一 第—傳動輪150設置於所述放送輪11與複數可導電之傳送 輪之間，用於將柔性基材自所述放送輪11傳送至所述複 099110241 表單蝙號A0101 第8頁/共22頁 0992018035-0 201134987 ❹ [0013] 數可導電之傳送払 堆 逑、 迓輪。所述至少一第二傳動輪151設置於所 複數數傳达輪與卷收輪12之間’用於將柔性基材自所述 少傳送輪傳送至所述卷收輪12。本實施例中，所述至 傳動輪150之數量為一個，其與所述第一傳送 140並排設置於 處 义所迷電鍍槽13之第一側132遠離底壁i3l ,丨、且與所述第一傳送輪140之間存於一定縫隙。所述至 第一傳動輪151之數量為兩個，並排設置於電鍍槽13 ”第傳送輪140同一深度處。所述兩個第二傳動輪 151之間存於—定縫隙。 所述可導電之傳動滾輪16設置於第二傳動輪151與複數傳 送輪之間’用於將柔性基材自卢斤述傳送輪傳送至所述第 -傳動輪151。所述傳動滾輪16之結構可與傳送輪之結構 相同。所述傳動滚輪16與第七傳送輪146並排設置於電鍍 槽13内同一深度處，且所述傳動滾輪16相較於所述第二 傳送輪141、第四傳送輪143與第六傳送輪145更靠近所 述至少一第二傳動輪151。 S. -；；, I 1 \ ：γ'' ;：；：：：：,；：/ ；' ϊ Ψ ^ [0014] 所述複數陽極板基本平行設置，且均浸沒於所述電鍍液 中。每一陽極板均具有相對之第一端170與第二端17][， 於任意相鄰之兩個陽極板中，一陽極板之第—端17〇與一 傳送輪相鄰另一陽極板之第二端171與另一傳送輪相鄰 ’從而使得柔性基材經過該兩個傳送輪時於該相鄰之兩 個陽極板之間傳送，所述複數陽極板用於作為陽極使得 於複數傳送輪之間傳送之柔性基材於導電狀況下進行電 鍍。本實施例中，所述複數陽極板均平行於所述電鑛槽 13之底壁131設置，每一陽極板之第一端17〇均位於電鍍 099110241 表單編號A0I01 第9頁/共22頁 0992018035-0 201134987 槽13内靠近第一側132處，第二端171均位於電鍍槽^内 靠近第二側13 3處。所述複數陽極板均採用不溶性陽極。 本實施例中，所述陽極板為表面鍍有金屬鈦之銅板。所 述複數陽極板等間距設置，相鄰之兩個陽極板之間之間 距等於所述傳送輪之直徑。每一傳送輪之中心均位於與 該傳送輪相鄰設置之陽極板所於之平面内。本實施例中 ’所述複數陽極板之數量為七個’分別為第一陽極板172 、第二陽極板173、第三陽極板174、第四陽極板175、 第五陽極板176、第六陽極板177與第七陽極板178。所 述第一陽極板172之第一端170與所述第一傳送輪14〇相 鄰，第一陽極板172之第二端171與第二傳送輪141平齊 。第一 IW極板173之第一端171與所述第二傳送輪mi相 鄰，第二陽極板173之第一瑞17〇與所述第一傳送輪14〇 平齊。所述第三陽極板174、第四陽極板175、第五陽極 板176與第六陽極板177之設置方式依次類推。所述第七 陽極板178之第一端170與第#傳送輪146相鄰。所述第 七陽極板I78之第二端17丨與第六.送丨鉍丨45平齊，所述 第七陽極板178之第二端171還與傳動滾輪16相鄰。 [0015] [0016] 可理解’所述電錢裝置還應包括電源與連接於所述電源 之正训器所述整流器可具有陽極輸出端與陰極輸出端 。所述複數傳送輪相互並聯，且均電連接於所述整流器 之陰極輸出端’從而可向所述柔性基材提供電流。所述 複數陽極板相互並聯’均電連接於整流器之陽極輸出端 〇 所述複數絕緣⑽所述電鑛槽13内 。每一絕緣隔 099110241 表單編號A0101 第10頁/共22頁 0992018035-0 201134987 板7連接於所述陽極板之第一端或第二端，用於隔開所 =陽極板與導電之傳送輪，以避免陽極板與傳送輪之間 路。具體地，每一絕緣隔板均垂直連接於所述陽極板 所述絕緣隔板於垂直於與該絕緣隔板對應之陽極板方 向之長度大於所述陽極板之厚度。所述複數絕緣隔板可 均為方形板體，可採用丙烯腈—丁二烯-苯乙烯（Ac_ 〇nitrile butadiene styrene，ABS)或聚氣乙 烯（Polyvinylchloride，PVC)製成。本實施例中， 〇 所述複數絕緣隔板之數量為八個，分別為第一絕緣隔板 180、第二絕緣隔板181、第三絕緣隔板i82、第四絕緣 隔板183、第五絕緣隔板ι84、第六絕緣隔板185、第七 絕緣隔板186與第八絕緣隔板187 ^第一絕緣隔板180位 於第—傳送輪140與第一陽極板172之第一端170之間。 第二絕緣隔板181位於第二傳送輪141與第二陽極板173 之第二端171之間》第三絕緣隔板182位於第三傳送輪 142與第三陽極板174之第一端170之間》四絕緣隔板 〇 183位於第四傳送輪143與第四_極板175之第二端171之 間。第五絕緣隔板184位於第五傳送輪144與第五陽極板 176之第一端17〇之間。第六絕緣隔板185位於第六傳送 輪145與第六陽極板177之第二端171之間。第七絕緣隔 板186位於第七傳送輪146與第七陽極板178之第一端170 之間。第八絕緣隔板187位於傳動滾輪16與第七陽極板 178之第二端171之間。 [0017] 當然，所述複數傳送輪及複數陽極板之數量不一定為七 個’複數絕緣隔板之數量不一定為八個，可視所述電鍍 099110241 表單編號A0101 第11頁/共22頁 0992018035-0 201134987 槽13之深度以及傳送輪之直徑大小作相應之設計。可理 解，傳送輪之數量越多，電鍍效率可提高之越多。 [0018] 當然，所述複數陽極板亦可均垂直於所述電鍍槽13之底 壁131所於之平面設置。或者所述複數陽極板亦可均於所 述電鍍槽13内傾斜設置，亦即，所述複數陽極板均與所 述電鍍槽13之底壁131所於之平面成一銳角或鈍角。 [0019] 所述陽離子補充槽19用於向所述電鍍槽13内提供陽離子 補充液。所述陽離子補充槽19具有一與所述電鍍槽13相 連通之輸送管190。本實施例中，所述陽離子補充槽19内 之陽離子補充液可為硫酸’硫酸可用於漆解氧化銅粉末 以獲得陽離子（銅離子）。 [00203 所述陽離子自動補充系統20包括陽離子濃度檢測器21、 控制器22與輸液泵23，如圖2所示。所述陽離子濃度檢測 器21位於所述電鍍槽13内，用於檢測所述電鍍槽内之陽 離子濃度。所述輸液泵23設置於所藥輸遂螫190。所述控 制器2 2用於接收所述陽離子濃度檢測器21之檢測結果並 於陽離子濃度低於預設值時控制所述輸液泵23開啟，從 而使所述陽離子補充槽19内之液體藉由所述輸送管190進 入電鍍槽13。 [0021] °月併參閱圖1至圖2，以下將以對柔性基材100進行電鍍 形成電錢銅層為例，說明本技術方p錢裝置10之使 用方法。 首先’提供柔性之柔性基材100。所述柔性基材〗00可為 兩個表面均形成有化學銅層之軟性姜#。所述柔性基材 099110241 表單編號40101 第〗2頁/共22頁 0992018035-0 [0022] 201134987 100主要捲繞於所述放送輪11，並有部分柔性基材100張 設於複數可導電之傳送輪、複數絕緣之傳動輪以及傳動 滾輪之間。具體地，柔性基材100之一端部穿過第一傳動 輪150與第一傳送輪140之間之縫隙，依次繞過第二傳送 輪141、第三傳送輪142、第四傳送輪143、第五傳送輪 144、第六傳送輪145、第七傳送輪146以及傳動滚輪16 ，最終穿過兩個第二傳動輪151之間之縫隙，到達卷收輪 12 ° 0 [0023] 然後，開啟電鍍裝置10之電源，同時傳輸柔性基材100， 對柔性基材100進行電鍍。 [0024] 以下將以捲繞於所述放送輪11之柔性基材100即將進入電 鍍槽13之一段為例，說明電鍍之過程。該段所述柔性基 材100於第一傳動輪150與第一傳送輪140之共同作用下 ，沿電鍍槽13之深度方向進入電鍍槽13。由於所述柔性 基材100表面之化學銅層内有電流通過，電鍍液中之銅離 子於柔性基材100表面附近發生還原反應得到銅單質，該 » 〇 銅單質逐漸沈積於柔性基材100表面。該段柔性基材100 經第一傳送輪140後，移動方向改為平行於電鍍槽13之底 壁131之第一方向XI。經過第二傳送輪141後，移動方向 改變了 180度，而沿平行於底壁131之第二方向X2移動。 該段柔性基材100經過第三傳送輪142後，又沿第一方向 XI移動，依次類推，經過第七傳送輪146後，柔性基材 100沿第一方向XI到達傳動滾輪16。經傳動滚輪16後， 該段柔性基材100基本完成電鍍，其移動方向改變90度， 而沿電鍍槽13之深度方向向遠離底壁131處移動，最終捲 099110241 表單編號 A0101 第 13 頁/共 22 頁 0992018035-0 201134987 燒於卷收輪12。 [0025] 該過程中，由於每一陽極板均與柔性基材1〇〇之表面平行 ，於電鍍過程中，柔性基枒1〇〇之同一表面各處電流密度 相等，從而形成之鍍層亦均勻。並且，由於沿電鍍槽13 之深度方向上，相鄰之兩個傳送輪之中心軸線之間距恰 等於所述傳送輪之直徑，且每一傳送輪均位於與之對應 之陽極板所於之平面内，每一陽極板與柔性基材1〇〇表面 之間距均為所述傳送輪之半徑，從而，於柔性基材1〇〇之 相對之兩個表面電流密度相等，從而形成之鍍層亦均勻 。同時’所述陽離子濃度檢測器21 —直於對電鍍槽13内 電鍍液中之銅離子濃度進行檢測，當控制器22計算出銅 離子濃度消耗至低於預設值時控制所述輸液泵23開啟’ 從而使所述陽離子補充槽19内之液體藉由所述輸送管J 9〇 進入電鑛槽13。所述電鍍槽13内之攪拌管134向電鑛槽 13内喷出氣體，可攪拌電鍍槽丨3内之電鍍液，使電鍍槽 13内各處銅離子濃度均勻化。 [0026] 本技術方案提供之電鑛裝置^善肴;；^數傳送輪，所述複數 傳送輪除了向柔性基材提供電流，還可移動電錢中之柔 性基材並改變柔性基材之移動方向，從而可使柔性基材 於電鍍槽内循環前進，充分利用電鍍槽之空間，提高電 鍍效率。此外，所述複數陽極板均平行於柔性基材，從 而柔性基材表面各處電流密度均相等，可提高電鍍之均 勻性。 综上所述’本發明確已符合發明專利之要件，遂依法提 出專利申請。惟，以上所述者僅為本發明之較佳實施方 099110241 表單編號A0101 第14頁/共22頁 0992018035-0 [0027] 201134987 式，自不能以此限制本案之申請專利範圍。舉凡熟悉本 案技藝之人士援依本發明之精神所作之等效修飾或變化 ，.皆應涵蓋於以下申請專利範圍内。 【圖式簡單說明】 [0028] 圖1係本技術方案實施例提供之電鍍裝置之結構示意圖。 [0029] 圖2係使用本技術方案實施例提供之電鍍裝置對柔性基材 進行電鍍之示意圖。 【主要元件符號說明】 〇 剛 電鍍裝置：10 [0031] 放送輪：11 [0032] 卷收輪：12 [0033] 電鍍槽：13 [0034] 侧壁：130 [0035] 底壁：131 〇 [0036] 第一側：132 [0037] 第二側：133 [0038] 攪拌管：134 [0039] 第一傳送輪： 140 [0040] 第二傳送輪： 141 [0041] 第三傳送輪： 142 [0042] 第四傳送輪： 143 099110241 表單編號A0101 第15頁/共22頁 0992018035-0 201134987 [0043] 第五傳送輪： 144 [0044] 第六傳送輪： 145 [0045] 第七傳送輪： 146 [0046] 第一傳動輪： 150 [0047] 第二傳動輪： 151 [0048] 傳動滾輪：16 [0049] 第一端：170 [0050] 第二端：171 [0051] 第一陽極板： 172 [0052] 第二陽極板： 173 [0053] 第三陽極板： 174 [0054] 第四陽極板： 175 [0055] 第五陽極板： 176 [0056] 第六陽極板： 177 [0057] 第七陽極板： 178 [0058] 第一絕緣隔板 ：180 [0059] 第二絕緣隔板 :181 [0060] 第三絕緣隔板 ：182 [0061] 第四絕緣隔板 ：183 099110241 表單編號A0101 第16頁/共22頁 0992018035-0 201134987 [0062] 第五絕緣隔板： 184 [0063] 第六絕緣隔板： 185 [0064] 第七絕緣隔板·· 186 [0065] 第八絕緣隔板： 187 [0066] 陽離子補充槽： 19 [0067] 輸送管：190 [0068] 陽離子自動補充系統：20 [0069] 陽離子濃度檢測器：21 [0070] 控制器：22 [0071] 輸液豕：2 3 [0072] 柔性基材：100 ❹ 099110241 表單編號A0101 第17頁/共22頁 0992018035-00992C 201134987 In the straight line of the circuit board to be mined, the material is increased by 34 materials. Therefore, the electricity money device needs to occupy a large amount of =, and the anode plate is arranged in such a way that the anode is to be plated away from the anode plate. 'Directly cause the board k to be unevenly plated. The conductive brush is used to conduct current to the surface of the circuit board to be plated: one; the surface 'small contact area' is not conducive to improving the efficiency of the money, and the other: the surface conductive brush itself will also deposit the money layer, and the conductive brush must be replaced after a period of time. [0004] [Draft] In view of this, it is necessary to provide a kind of electric power to save rhyme and improve the uniformity of electric bonds and the efficiency of electric ore. [0005] A plating apparatus for electroplating a continuously conveyed flexible substrate. The electroplating apparatus includes a discharge wheel, a take-up reel, an electro-recording tank containing a plating solution, a plurality of electrically conductive transfer wheels, and a plurality of anode plates. The delivery wheel and the take-up reel are both disposed outside the electric f-mine. The plurality of transfer wheels and the plurality of anode plates are disposed in the plating tank. The plurality of anode plates and the plurality of electrically conductive transfers are all immersed in the plating solution. The delivery wheel is used to deliver a flexible substrate into the plating bath. The plurality of transfer wheels are used to transfer the flexible substrate that carries the delivery wheel to the take-up reel by rotation and to conduct electricity to the flexible substrate being conveyed. The plurality of anode plates are arranged substantially in parallel. Each anode plate has opposite first and second ends. In any two adjacent anode plates, the first ends of the two anode plates are adjacent, and the second ends of the two anode plates are adjacent. The first end of an anode plate is adjacent to a transfer wheel and the second end of the other anode plate is adjacent to another transfer wheel. The flexible substrate is transferred between the two adjacent anodes 099110241 Form No. A0101 Page 5 of 22 0992018035-0 201134987 when passing through the two transfer wheels. The plurality of anode plates are used as an anode to electroplate the flexible substrate transferred between the plurality of transfer wheels under conductive conditions. The take-up reel is used to rewind the plated flexible substrate from a plurality of transfer wheels. [0007] [0007] [0007] The electroplating apparatus of the electroplating apparatus of the present technical device has a plurality of transfer wheels, which can move the flexible substrate in the electroplating and change in addition to supplying current to the flexible substrate. The flexible substrate moves in the direction of the flexible substrate, so that the flexible substrate can be used in the electric ore tank, and the space of the keyway can be fully utilized to improve the efficiency of the key. In addition, the plurality of anode plates are all parallel to the flexible substrate' so that the current densities are equal across the surface of the flexible substrate, which improves the uniformity of the ore. [Embodiment] Hereinafter, an electric ore device of the present technical solution will be described in detail with reference to the accompanying drawings and embodiments. Referring to FIG. 1 , the technical solution introduces m kinds of electric recording devices, which are used for conducting electric ore on a continuous flexible substrate. The flexible substrate is a flexible material. The electric forging device 10 comprises a feeding wheel 11, a winding wheel 12, a plating tank 13 containing a plating solution, a plurality of electrically conductive transmission wheels, a plurality of insulated transmission wheels, an electrically conductive transmission roller, and a plurality of anodes. Plate, complex insulation separator, - cation replenishing tank 19 and - cation automatic replenishment system 2 〇. The plating solution may be a mixture containing copper sulfate, sulfuric acid, hydrochloric acid, or the like. The delivery wheel 11 and the take-up reel 12 are located outside the plating tank 13. The delivery wheel n-shaped the (four) substrate and shouts the flexible base 099110241 to the electrical storage 13 . The take-up reel 12 is used for winding a substrate which has been electroplated from the plating tank 0992018035-0 201134987 13 from the drop-off wheel u form number A0101, page 6 / page 22. That is, the flexible substrate can enter the plating tank 13 from the delivery wheel 11 and be output to the take-up reel 12 after being completed and rolled up by the take-up reel 12. [0010] The plating tank 13 may be a rectangular tank body whose one end is not sealed, and includes a connecting side wall 130 and a bottom wall 131. The plating bath 13 has an opposite first side 132 and a second side 133. In this embodiment, the delivery wheel 11 and the take-up reel 12 are respectively adjacent to the first side 132 and the second side 133. Preferably, a stirring tube 134 is disposed in the plating tank 13 near the bottom wall 131, and the 0 stirring tube 134 is used for discharging gas into the plating tank 13 to stir the plating liquid in the plating tank 13. [0011] The plurality of electrically conductive transfer wheels are all immersed in the plating solution. The plurality of electrically conductive transfer wheels are each used to transfer a flexible substrate that transports the delivery wheel 11 to the take-up reel 12 and to conduct a flexible substrate for transfer. Each of the transfer wheels includes a transfer shaft and a pulley sleeved on the transfer shaft. The transmission shaft of the plurality of transmission wheels can be mechanically smashed by gears or belts: &; 151 鳃 f f f f f f f f f , , , , , , , , , , ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ > I — * · / r , ▼ ▼ , * · I - o Rotate at the same speed. Each roller can be rotated by the corresponding transmission shaft. The roller is made of stainless steel and its surface is plated with titanium metal to prevent the roller itself from depositing a plating layer. In this embodiment, the plurality of transfer wheels are alternately distributed in the plating tank 13 along the depth direction of the plating bath 13 on the first side 132 and the second side 133. The number of the plurality of transfer wheels is seven, which are a first transfer wheel 140, a second transfer wheel 141, a third transfer wheel 142, a fourth transfer wheel 143, a fifth transfer wheel 144, a sixth transfer wheel 145, and a Seven transfer wheels 146. The first transfer wheel 140, the third transfer wheel 142, the fifth transfer wheel 144 and the seventh transfer wheel 146 099110241 form number A0101 page 7 / total 22 page 0992018035-0 201134987 are arranged in parallel in the plating tank 13 - The side, and the centers of the first to fourth transfer wheel (4), the third transfer wheel 142, the fifth transfer wheel 144 and the seventh transfer wheel 146 are all located on a straight line. The second transfer wheel 141, the fourth transfer wheel 143 and the sixth transfer wheel 145 are both disposed on the second side 133 of the electric ore tank 13. The t-centers of the second transfer wheel 141, the fourth transfer wheel 143, and the sixth transfer wheel 145 are all located on a straight line. In the first conveying wheel, the third conveying wheel 142, the fifth conveying wheel 144 and the seventh conveying wheel 146, the distance between the centers of the two conveying wheels adjacent in the depth direction of the plating tank 13 is the diameter of the conveying wheel Doubled. In the second transfer wheel 141, the fourth transfer wheel 143 and the sixth transfer wheel 145, the distance between the centers of the two transfer wheels adjacent in the depth direction of the plating tank 13 is twice the diameter of the transfer wheel. The plurality of transfer wheels are equal in diameter, and the distance between the central axes of the adjacent two transfer wheels is exactly equal to the diameter of the transfer wheel in the depth direction of the plating tank 13. For example, the distance between the second transfer wheel 141 and the first transfer wheel 140 in the axial direction of the plating tank 13 is equal to the diameter of the transfer wheel. Therefore, in the present embodiment, the moving direction of the soft substrate in the plating tank 13 is parallel to the flat wall 131. [0012] The plurality of insulated transmission wheels are all located in the plating tank 13. The structure of the plurality of transfer wheels is substantially the same as that of the drive wheels, and the transmission line speed of the plurality of transfer wheels is equal to the transmission line speed of the plurality of drive wheels. If the plurality of transfer wheels share a drive with the drive wheels, the plurality of transfer wheels have the same diameter as the drive wheels, and the plurality of drive wheels includes at least a first drive wheel 150 and at least a second drive wheel 151. The at least one first transmission wheel 150 is disposed between the delivery wheel 11 and the plurality of electrically conductive transfer wheels for transferring the flexible substrate from the delivery wheel 11 to the complex 099110241 form bat number A0101. Page / Total 22 pages 0992018035-0 201134987 ❹ [0013] The number of conductive transmission 払 stacking, 迓 wheel. The at least one second drive wheel 151 is disposed between the plurality of transfer wheels and the take-up reel 12 for transferring a flexible substrate from the less transfer wheel to the take-up reel 12. In this embodiment, the number of the driving wheels 150 is one, and the first side 132 of the plating tank 13 disposed side by side with the first conveying 140 is away from the bottom wall i3l, and There is a certain gap between the first transfer wheels 140. The number of the first transmission wheels 151 is two, and is arranged side by side at the same depth of the plating tank 13" of the transfer wheel 140. The two second transmission wheels 151 are disposed between the two slits. The drive roller 16 is disposed between the second transmission wheel 151 and the plurality of transfer wheels for transmitting the flexible substrate from the transfer wheel to the first drive wheel 151. The structure of the drive roller 16 can be combined with the transfer wheel The drive roller 16 is disposed side by side with the seventh transfer wheel 146 at the same depth in the plating tank 13, and the drive roller 16 is compared with the second transfer wheel 141, the fourth transfer wheel 143 and the sixth. The transfer wheel 145 is closer to the at least one second transmission wheel 151. S. -;;, I 1 \ : γ'' ;:;::::,;:/ ;' ϊ Ψ ^ [0014] The anode plates are arranged substantially in parallel and are immersed in the plating solution. Each anode plate has a first end 170 and a second end 17] [, in any two adjacent anode plates, an anode plate The first end 17 is adjacent to a transfer wheel and the second end 171 of the other anode plate is adjacent to the other transfer wheel. Thereby transferring the flexible substrate between the two adjacent anode plates through the two transfer wheels, the plurality of anode plates being used as an anode to allow the flexible substrate to be transferred between the plurality of transfer wheels under conductive conditions In the embodiment, the plurality of anode plates are disposed parallel to the bottom wall 131 of the electric ore tank 13, and the first end 17〇 of each anode plate is located on the plating 099110241 Form No. A0I01 Page 9 / Total 22 pages 0992018035-0 201134987 The groove 13 is located near the first side 132, and the second end 171 is located in the plating tank ^ near the second side 13 3. The plurality of anode plates are all made of an insoluble anode. In this embodiment, The anode plate is a copper plate whose surface is plated with titanium metal. The plurality of anode plates are equally spaced, and the distance between two adjacent anode plates is equal to the diameter of the transfer wheel. The center of each transfer wheel is located at The anode plate of the transfer wheel is disposed in a plane. In the embodiment, the number of the plurality of anode plates is seven, which are a first anode plate 172, a second anode plate 173, and a third anode plate 174, respectively. a fourth anode plate 175, a fifth anode plate 176, a sixth anode plate 177 and a seventh anode plate 178. The first end 170 of the first anode plate 172 is adjacent to the first transfer wheel 14A, and the second anode plate 172 is second. The end 171 is flush with the second transfer wheel 141. The first end 171 of the first IW plate 173 is adjacent to the second transfer wheel mi, and the first transfer of the second anode plate 173 and the first transfer The wheel 14 is flush. The third anode plate 174, the fourth anode plate 175, the fifth anode plate 176 and the sixth anode plate 177 are arranged in the same manner. The first end 170 of the seventh anode plate 178 is The ## transfer wheel 146 is adjacent. The second end 17 of the seventh anode plate I78 is flush with the sixth feed port 45, and the second end 171 of the seventh anode plate 178 is also adjacent to the drive roller 16. [0016] It will be understood that the electric money device should also include a power source and a positive train connected to the power source. The rectifier may have an anode output and a cathode output. The plurality of transfer wheels are connected in parallel with each other and are each electrically coupled to a cathode output end of the rectifier to provide current to the flexible substrate. The plurality of anode plates are electrically connected in parallel to each other and are electrically connected to the anode output end of the rectifier 〇 the plurality of insulations (10) in the electric ore tank 13. Each insulation spacer 099110241 Form No. A0101 Page 10 / Total 22 Page 0992018035-0 201134987 The board 7 is connected to the first end or the second end of the anode plate for separating the anode plate and the conductive transfer wheel. To avoid the path between the anode plate and the transfer wheel. Specifically, each of the insulating spacers is vertically connected to the anode plate. The length of the insulating spacer in a direction perpendicular to the anode plate corresponding to the insulating spacer is greater than the thickness of the anode plate. The plurality of insulating spacers may each be a square plate body, and may be made of acrylonitrile-butadiene-styrene (ABS) or polyvinyl chloride (PVC). In this embodiment, the number of the plurality of insulating spacers is eight, which are a first insulating spacer 180, a second insulating spacer 181, a third insulating spacer i82, a fourth insulating spacer 183, and a fifth. The insulating spacer ι 84, the sixth insulating spacer 185, the seventh insulating spacer 186 and the eighth insulating spacer 187 ^ the first insulating spacer 180 is located at the first end 170 of the first transfer wheel 140 and the first anode plate 172 between. The second insulating spacer 181 is located between the second transfer wheel 141 and the second end 171 of the second anode plate 173. The third insulating spacer 182 is located at the first end 170 of the third transfer wheel 142 and the third anode plate 174. The fourth insulating spacer 183 is located between the fourth transfer wheel 143 and the second end 171 of the fourth_pole plate 175. A fifth insulating spacer 184 is located between the fifth transfer wheel 144 and the first end 17〇 of the fifth anode plate 176. The sixth insulating spacer 185 is located between the sixth transfer wheel 145 and the second end 171 of the sixth anode plate 177. A seventh insulating spacer 186 is located between the first transfer wheel 146 and the first end 170 of the seventh anode plate 178. The eighth insulating spacer 187 is located between the drive roller 16 and the second end 171 of the seventh anode plate 178. [0017] Of course, the number of the plurality of transfer wheels and the plurality of anode plates is not necessarily seven, and the number of the plurality of insulating spacers is not necessarily eight, as shown in the above-mentioned plating 099110241 Form No. A0101 Page 11 / Total 22 Page 0992018035 -0 201134987 The depth of the groove 13 and the diameter of the transfer wheel are designed accordingly. It can be understood that the more the number of transfer wheels, the more the plating efficiency can be improved. [0018] Of course, the plurality of anode plates may also be disposed perpendicular to the plane of the bottom wall 131 of the plating tank 13. Alternatively, the plurality of anode plates may be disposed obliquely in the plating tank 13, that is, the plurality of anode plates are at an acute or obtuse angle with the plane of the bottom wall 131 of the plating tank 13. [0019] The cation replenishing tank 19 is for supplying a cation replenishing liquid into the plating tank 13. The cation replenishing tank 19 has a transfer pipe 190 that communicates with the plating tank 13. In this embodiment, the cation replenishing liquid in the cation replenishing tank 19 may be sulfuric acid. Sulfuric acid may be used to lacquer the copper oxide powder to obtain a cation (copper ion). [00203] The cation auto-replenishment system 20 includes a cation concentration detector 21, a controller 22, and an infusion pump 23, as shown in FIG. The cation concentration detector 21 is located in the plating tank 13 for detecting the concentration of cations in the plating bath. The infusion pump 23 is disposed on the drug delivery 190. The controller 22 is configured to receive the detection result of the cation concentration detector 21 and control the infusion pump 23 to be turned on when the cation concentration is lower than a preset value, so that the liquid in the cation replenishing tank 19 is caused by The delivery tube 190 enters the plating bath 13. [0021] Referring to FIG. 1 to FIG. 2, the method of using the flexible substrate 100 to form a battery copper layer will be exemplified below. First, a flexible flexible substrate 100 is provided. The flexible substrate 00 can be a soft ginger # having a chemical copper layer formed on both surfaces. The flexible substrate 099110241 Form No. 40101 No. 2 page / Total 22 pages 0992018035-0 [0022] 201134987 100 is mainly wound around the delivery wheel 11, and a part of the flexible substrate 100 is stretched in a plurality of conductive transmission Between the wheel, the plurality of insulated transmission wheels and the drive roller. Specifically, one end of the flexible substrate 100 passes through the gap between the first transmission wheel 150 and the first transfer wheel 140, and sequentially bypasses the second transfer wheel 141, the third transfer wheel 142, the fourth transfer wheel 143, and the The fifth transfer wheel 144, the sixth transfer wheel 145, the seventh transfer wheel 146, and the drive roller 16 finally pass through the gap between the two second drive wheels 151 to reach the take-up reel 12 ° 0 [0023] Then, the plating is turned on. The power source of the device 10 simultaneously transports the flexible substrate 100 to electroplate the flexible substrate 100. [0024] Hereinafter, the process of electroplating will be described by taking a section in which the flexible substrate 100 wound around the discharge wheel 11 is about to enter the electroplating bath 13 as an example. The flexible substrate 100 of the section enters the plating tank 13 in the depth direction of the plating tank 13 under the action of the first transmission wheel 150 and the first transfer wheel 140. Since a current flows in the chemical copper layer on the surface of the flexible substrate 100, copper ions in the plating solution are reduced in the vicinity of the surface of the flexible substrate 100 to obtain a simple substance of copper, which is gradually deposited on the surface of the flexible substrate 100. . After the flexible substrate 100 passes through the first transfer wheel 140, the moving direction is changed to be parallel to the first direction XI of the bottom wall 131 of the plating bath 13. After passing through the second transfer wheel 141, the moving direction is changed by 180 degrees and moved in the second direction X2 parallel to the bottom wall 131. After the flexible substrate 100 passes through the third transfer wheel 142, it moves in the first direction XI, and so on. After passing through the seventh transfer wheel 146, the flexible substrate 100 reaches the drive roller 16 in the first direction XI. After the drive roller 16, the flexible substrate 100 is substantially plated, and its moving direction is changed by 90 degrees, and moves away from the bottom wall 131 in the depth direction of the plating tank 13, and finally rolls 099110241 Form No. A0101 Page 13 22 pages 0992018035-0 201134987 Burned on the reeling wheel 12. [0025] In this process, since each anode plate is parallel to the surface of the flexible substrate 1 ,, during the electroplating process, the current density of the same surface of the flexible substrate is equal, so that the plating layer is uniform. . Moreover, since the distance between the central axes of the adjacent two transfer wheels is exactly equal to the diameter of the transfer wheel in the depth direction of the plating tank 13, and each transfer wheel is located on the plane of the corresponding anode plate The distance between each anode plate and the surface of the flexible substrate is the radius of the transfer wheel, so that the current density of the opposite surfaces of the flexible substrate 1 is equal, so that the plating layer is uniform. . At the same time, the cation concentration detector 21 directly detects the concentration of copper ions in the plating solution in the plating bath 13, and controls the infusion pump 23 when the controller 22 calculates that the copper ion concentration is consumed below a preset value. Turning on 'so that the liquid in the cation replenishing tank 19 enters the electric ore tank 13 through the conveying pipe J 9 . The stirring pipe 134 in the plating tank 13 ejects gas into the electric ore tank 13, and the plating liquid in the plating tank 3 can be stirred to make the copper ion concentration in the plating tank 13 uniform. [0026] The electromechanical device provided by the technical solution is a good transfer device; the plurality of transfer wheels, in addition to supplying current to the flexible substrate, can also move the flexible substrate in the electric money and change the flexible substrate. The direction of movement allows the flexible substrate to circulate in the plating bath, making full use of the space of the plating bath and improving the plating efficiency. In addition, the plurality of anode plates are parallel to the flexible substrate, so that the current density is equal across the surface of the flexible substrate, which improves the uniformity of plating. In summary, the present invention has indeed met the requirements of the invention patent and has filed a patent application in accordance with the law. However, the above is only the preferred embodiment of the present invention. 099110241 Form No. A0101 Page 14 of 22 0992018035-0 [0027] 201134987, which cannot limit the scope of patent application in this case. Equivalent modifications or variations made by persons skilled in the art in light of the spirit of the invention are intended to be included within the scope of the following claims. BRIEF DESCRIPTION OF THE DRAWINGS [0028] FIG. 1 is a schematic structural view of a plating apparatus provided by an embodiment of the present technical solution. 2 is a schematic view of electroplating a flexible substrate using a plating apparatus provided by an embodiment of the present technical solution. [0029] FIG. [Main component symbol description] 〇刚 plating device: 10 [0031] Delivery wheel: 11 [0032] Rewinding wheel: 12 [0033] Plating tank: 13 [0034] Side wall: 130 [0035] Bottom wall: 131 〇 [ 0036] First side: 132 [0037] Second side: 133 [0038] Mixing tube: 134 [0039] First transfer wheel: 140 [0040] Second transfer wheel: 141 [0041] Third transfer wheel: 142 [ 0042] Fourth transfer wheel: 143 099110241 Form number A0101 Page 15/Total 22 page 0992018035-0 201134987 [0043] Fifth transfer wheel: 144 [0044] Sixth transfer wheel: 145 [0045] Seventh transfer wheel: 146 [0046] First transmission wheel: 150 [0047] Second transmission wheel: 151 [0048] Transmission roller: 16 [0049] First end: 170 [0050] Second end: 171 [0051] First anode plate: 172 Second anode plate: 173 [0053] Third anode plate: 174 [0054] Fourth anode plate: 175 [0055] Fifth anode plate: 176 [0056] Sixth anode plate: 177 [0057] Anode plate: 178 [0058] First insulating spacer: 180 [0059] Second insulating spacer: 181 [0060] Third insulating spacer: 182 [00 61] Fourth Insulation Partition: 183 099110241 Form No. A0101 Page 16 / Total 22 Page 0992018035-0 201134987 [0062] Fifth Insulation Partition: 184 [0063] Sixth Insulation Partition: 185 [0064] Seventh Insulation Separator · · 186 [0065] Eightth Insulation Partition: 187 [0066] Cation Supplementation Tank: 19 [0067] Delivery Tube: 190 [0068] Cation Automated Replenishment System: 20 [0069] Cation Concentration Detector: 21 [0070 ] Controller: 22 [0071] Infusion 豕: 2 3 [0072] Flexible substrate: 100 ❹ 099110241 Form number A0101 Page 17 of 22 0992018035-0