1342900 九、發明說明： 【發明所屬之技術領域】 本發明係有關於一種金屬箔電解製造裝置，其包括使 金屬猪通電的旋轉陰極筒以及與該旋轉陰極筒相向的陽 極，將電解液連續地供給至旋轉陰極筒與陽極之間，同時 使旋轉陰極筒上的金屬通電。 【先前技術】 f知的金^電解製造裝置具有難以使供給的電解液 ，的流動平均而得到平均之厚度的金屬落的問題。為了解決 以下的問題而提出以下的專利文獻所記載的發明。 、 [專利文獻1]特許第3150814號 上述專利文獻1所記載的發明中，將電解液連續地供 給至旋轉陰極筒與陽極之間的電解液供給裝置的電解液供 給口係與旋轉圓筒陰極的旋轉轴方向平行而呈狹縫狀，從 旋轉圓筒陰極的下方開口於上诚門陆 π上迷間隙，而且在電解液供給 口上’橫越使金屬箔通電的赏声 电幻見度Q間中設有複數個電解液 流量調節裝置。 [發明所欲解決的問題] 專利文獻1記載的雷艇油舰彡人 冤解液供給口係藉由橫越寬度區間 的複數個電解液流量裝置而纲銘故 衣直而調卽流量，因此由開口部供給 的電解液的流動是不平均的，右 有…、法平均地供給至旋轉圓 筒陰極表面的問題。又，选虹β 喊又複數個電解液流量調節裝置由於 構造複雜而不實用。 【發明内容】BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a metal foil electrolytic manufacturing apparatus including a rotating cathode barrel that energizes a metal pig and an anode that faces the rotating cathode barrel, continuously discharging the electrolyte It is supplied between the rotating cathode barrel and the anode while energizing the metal on the rotating cathode barrel. [Prior Art] The gold electrolysis production apparatus of the present invention has a problem that it is difficult to average the flow of the supplied electrolyte solution to obtain an average thickness of the metal. In order to solve the following problems, the invention described in the following patent documents is proposed. In the invention described in Patent Document 1 of the Japanese Patent Application No. 3150814, the electrolyte solution is continuously supplied to the electrolyte supply port of the electrolyte supply device between the rotary cathode can and the anode, and the rotary cylinder cathode The direction of the rotation axis is parallel and slit-like, and the gap is opened from the lower side of the cathode of the rotating cylinder to the upper gate π, and the sound audibility of the metal foil is traversed on the electrolyte supply port. There are a plurality of electrolyte flow regulating devices in between. [Problems to be Solved by the Invention] The Thunderboat Oil Tanker's sputum supply port described in Patent Document 1 uses a plurality of electrolyte flow rate devices across the width section to illuminate the flow rate. The flow of the electrolytic solution supplied from the opening portion is not uniform, and there is a problem that the method is supplied to the surface of the rotating cylindrical cathode on the right. In addition, the selection of the rainbow β shouting and multiple electrolyte flow regulating devices is not practical due to the complicated structure. [Summary of the Invention]
2048-8475-PF 5 1342900 以複數根螺检5 9固定的1 —4* M 疋的調卽機構。該調節機構 54的端部等適當的位置 5 以础 穿5又縱方向的長孔60，使螺栓 59鎖入該長孔6〇中，在今伙 節板54… 在該長孔6〇的範圍内’上下移動調 卵板54而疋位的裝置。藉此， 产。 曰田殳更液供給口6的寬 在該調節機構的作用下，電解 电解及的供給量可容易且確 實地被調節，同時可改變個丨戈 又變個別來自開口部的液供給量的平 衡。2048-8475-PF 5 1342900 The 11*4* M 固定 adjustment mechanism with a fixed number of 5 9 screws. An appropriate position 5 of the end portion of the adjusting mechanism 54 is inserted through the long hole 60 in the longitudinal direction of the 5 and the longitudinal direction, so that the bolt 59 is locked into the long hole 6〇, and in the long hole 6 A device that moves the turbinate 54 up and down in the range. By this, production. Under the action of the adjustment mechanism, the supply amount of the electrolysis and electrolysis can be easily and surely adjusted, and at the same time, the balance of the liquid supply amount from the opening portion can be changed. .
第7圖為上述減壓機構7的第二實施例的移除一部份 的立體圖。該減魔機構7係將表面穿設有複數個狹縫72a 的狹縫板72 ^過—片側板5!的全長而將兩端密接於側板 51而安裝的機構。 根據該狹縫板72，電解液由狭縫72a通過窄化的液流 路而從下側的液室R1朝上側的液室R3流出，因此電解液 成為平均的壓力及平均的速度而輸送至上側的液室⑽。 又，雖然未圖示，取代上述狹縫板72，也可使用遮蔽 板、孔口等作為減壓裝置。 第8圖為上述減壓機構7的第三實施例的剖面正視 圖。該減壓機構7將多孔質材料所構成的板材73橫過二片 側板51的全長而將兩端密接於側板51而安裴的機構。 根據該板材73 ’電解液通過板材73從下側的液室R1 朝上側的液室R3流出時，由於電解液通過多數個孔而達到 平均的壓力及平均的流速而輸送至上側的液室R3。 第9圖為上述減壓機構7的第四實施例的剖視圖。該Fig. 7 is a perspective view showing a part of the removal of the second embodiment of the above-described pressure reducing mechanism 7. The enchantment mechanism 7 is a mechanism in which the surface of the slit plate 72 of the plurality of slits 72a is passed through the entire length of the sheet-side plate 5, and the both ends are closely attached to the side plate 51. According to the slit plate 72, the electrolytic solution flows out from the lower liquid chamber R1 toward the upper liquid chamber R3 through the narrowed liquid flow path by the slit 72a, so that the electrolytic solution is transported to the upper pressure and the average speed. Side liquid chamber (10). Further, although not shown, instead of the slit plate 72, a shielding plate, an orifice, or the like may be used as the pressure reducing means. Fig. 8 is a cross-sectional front view showing the third embodiment of the pressure reducing mechanism 7 described above. The pressure reducing mechanism 7 has a mechanism in which the plate material 73 made of a porous material is traversed over the entire length of the two side plates 51, and both ends are in close contact with the side plates 51. When the electrolyte plate 73' flows out from the lower liquid chamber R1 toward the upper liquid chamber R3 through the plate material 73, the electrolyte is supplied to the upper liquid chamber R3 by the average pressure and the average flow rate through the plurality of holes. . Fig. 9 is a cross-sectional view showing a fourth embodiment of the pressure reducing mechanism 7 described above. The
2048-8475-PF 11 1342900 減壓機構7將具有空隙的填充材料所構成的板材74橫過二 片側板51的全長而將兩端密接於侧板51而安裝的機構。 根據該板材74，電解液通過板材74從下側的液室Ri 朝上側的液室R3流出時，由於電解液通過多數個孔而達到 平均的壓力及平均的流速而輸送至上側的液室r3。2048-8475-PF 11 1342900 The pressure reducing mechanism 7 is a mechanism in which a plate material 74 made of a filler having a gap is placed across the entire length of the two side plates 51, and both ends are in close contact with the side plates 51. According to the plate member 74, when the electrolyte solution flows out from the lower liquid chamber Ri to the upper liquid chamber R3 through the plate member 74, the electrolyte is supplied to the upper liquid chamber r3 by the average pressure and the average flow rate through the plurality of holes. .
第1 0圖為上述減壓機構7的第五實施例的剖視圖。在 本實施例中’將上述實施例1的板材71二片平行配置，由 該二片板材71將給液裝置5分成三部分，形成下側的液室 R1、中間的液室R2以及上側的液室R3，使液室R3的寬度 比液室R2的寬度窄。 根據此減壓機構，與上述實施例1的減壓機構相比， 電解液由於二片板材71可有效地達到平均的壓力及平均 的流速。 【圖式簡單說明】 第1圖為第一實施例的金屬箔電解製造裝置的概略剖 視側視圖。 第2圖為液供給裝置的剖面正視圖。 第3圖為第2圖中沿ϊ丨丨-〗π線的剖面放大圖。 第4圖為液供給口移除一部份的立體圖。 第5圓為表示液供給口的第二實施例的移除一部份的 正視圖。 立體圖 第6圖為表示液供給口的第三實施例的移除一部份的 癌I 〇Fig. 10 is a cross-sectional view showing a fifth embodiment of the pressure reducing mechanism 7 described above. In the present embodiment, two sheets 71 of the above-described first embodiment are arranged in parallel, and the liquid supply device 5 is divided into three portions by the two sheets 71, and the liquid chamber R1 on the lower side, the liquid chamber R2 in the middle, and the upper side are formed. The liquid chamber R3 has a width of the liquid chamber R3 that is narrower than the width of the liquid chamber R2. According to this pressure reducing mechanism, the electrolyte solution can effectively achieve an average pressure and an average flow rate due to the two sheets 71 as compared with the pressure reducing mechanism of the above-described first embodiment. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic cross-sectional side view showing a metal foil electrolytic manufacturing apparatus of a first embodiment. Fig. 2 is a cross-sectional front view of the liquid supply device. Fig. 3 is an enlarged cross-sectional view taken along line ϊ丨丨-〗 π in Fig. 2. Figure 4 is a perspective view of a portion of the liquid supply port removed. The fifth circle is a front view showing a part of the removal of the second embodiment of the liquid supply port. Fig. 6 is a view showing a third embodiment of the liquid supply port for removing a part of the cancer I 〇
圖為表 示減壓機構的第二實施例 的移除一部份的The figure shows a part of the removal of the second embodiment of the pressure reducing mechanism
2048-8475-PF 12 1342900 立體圖。 第8圖為減壓機構的第三實施例的剖視圖。 第9圖為減壓機構的第四實施例的剖視圖。 第1 0圖為減壓機構的第五實施例的剖視圖。 【主要元件符號說明】 A〜金屬箔電解製造裝置； 1〜旋轉陰極筒； 2〜陽極；2048-8475-PF 12 1342900 perspective view. Figure 8 is a cross-sectional view showing a third embodiment of the pressure reducing mechanism. Figure 9 is a cross-sectional view showing a fourth embodiment of the pressure reducing mechanism. Fig. 10 is a cross-sectional view showing a fifth embodiment of the pressure reducing mechanism. [Main component symbol description] A ~ metal foil electrolytic manufacturing device; 1 ~ rotating cathode tube; 2 ~ anode;
4〜液流入口； 5〜給液裝置； 6〜液供給口； 7〜減壓裝置； 8〜液流通路； 13〜電解槽； 51〜側板； 52〜頂版； 5 4〜調節板； 59〜螺栓； 6 0〜長孔； 71、73、74〜板材； 7 2〜狹縫板； 7 2 a〜狹縫； 7 3〜板材； 74〜板材； 134~ liquid inlet; 5~ liquid supply device; 6~ liquid supply port; 7~ decompression device; 8~ liquid flow path; 13~ electrolytic cell; 51~ side plate; 52~ top plate; 59~Bolt; 6 0~ long hole; 71, 73, 74~ plate; 7 2~ slit plate; 7 2 a~slit; 7 3~ plate; 74~ plate;
2048-8475-PF2048-8475-PF