M284436 八、新型說明： 【新型所屬之技術領域】 本創作係關於-種可將㈣與液體充分混合之反應槽，尤指一種 透過物理方法可使液體（自來水）内之氣體（臭氧)含量增加，達到具有 更高氣液混合之溶解率，提高殺菌與消毒作用之一種氣液反應槽。 【先前技術】 習用所知’藉由-種臭氧產生器，可以提供生成臭氧氣體，而臭 氧可以消滅細菌達到祕、除臭之作用亦是麵週知，本案創作人曾 發明創作一種混合器⑴(請參閱第一囷），令液體α)(即一般之自I 水)與由-臭氧產生器（圖未示出）所送進來的臭氧⑽同時通過該混 合器⑴後，送出來的液體⑹内則含有臭氧⑽，可以用來進行清洗 衣物、蔬果時，提供殺菌、消毒、去除農藥與臭味等功效；惟該等 臭氧產生器因為構件特殊’生成產生臭氧時又必須耗費高能量，臭氧 得來不易，又如何能要求於液體内含有較高濃度之臭氧，以提高其殺 菌消毒作用，更如何能應付-般之民生需求，長期、大量的使用。 【新型内容】 有鑑於，欲提高於液體内臭氧的濃度，亦即提高殺菌的速度與功 效，關鍵在於液體與臭氧接觸反應之時間，乃研發出—種以物理方 法，使液體氣泡化而增加與臭氧氣體之接觸面積，卩及利用層層迴 流設計，減反狀刺，增加液雜臭魏航合之時間可ς高 氣液混合之速度以及溶解率。 m 本創作-種氣液混合反應槽，設有―人口與—出σ，該入口係供 M284436 已含有臭氧之液體進入，該出口則供進入反應槽作用後之液體輸出； 該反應槽内設置有若干層之反應流道，各該反應流道係於交錯位置設 置無數、細小之流通孔以流通’使液體氣泡化增加與臭氧氣體之接觸 面積’層層迴流設計則可產生滯流效果，增加液體與臭氧氣體混.合之 時間，藉以提高氣液混合之速度以及溶解率，而能提高殺菌功效者。 【實施方式】 本創作一種氣液混合反應槽（20)，請參閱第二圖與第三圖所示， φ 係為一呈圓管狀之槽體(23)，具有一入口（25)與一出口（27)，該入口 (25)係供已含有臭氧(〇3)之液體(L)(一般之自來水）進入，即指將液體 (一般之自來水）先行通過一種混合器（如第一圖所示）後，變成為液體 (L)内含有臭氧(03)之液體(L+03)進入於槽體(23)内再反應；該出口 (27)則供進入本創作之反應槽（20)作用後、内含高濃度臭氧之液體(力） 輸出； 又’本創作反應槽(20)之该槽體(23)，請配合參閱第三圖與第四 # _示，係藉由-層-層之環狀管壁⑽〜(34)區隔形成若干之反紐 道(35)〜(39)，作為供液體流通之通路；而，該入口（25)係設於第一層 (最外圈)之環狀管壁⑽上方，接著於該第二層之環狀管壁⑻下^ 則設有複數、孔徑相當細小（約介於6mm〜12mm之間） 於第三層之雜管壁⑽认歧有魏 (321)，依序於該第四層之環狀管壁⑽下方、第五層環狀管壁⑽ 之上方’以-層於上方，接著下-胁下方交錯之方式分設複數之流 通孔(331)、（341)，而於最後-®之反應流道⑽下方、錯開該環狀 5 M284436 管壁（34)於上方設置流通孔（341)之位置處則設置該出口（27)。 藉由以上之設計，由本創作反應槽（20)上方之入口（25)進入於槽 體(23)内含有較低濃度量臭氧(〇3)之液體(L+03)，先經由該第一反應 流道(35)往下，並透過設置於第二層之環狀管壁（31)下方複數之流通 孔(311)進入該第二反應流道(35)内，接著再由該第二反應流道(36) 往上，透過設置於第三層環狀管壁（32)上方複數之流通孔（321)進入於 該第二反應流道(37)内，>f主下透過設置於第三層之環狀管壁（33)卞方 複數之流通孔(331)入該第四反應流道(38)往上，透過設置於第四層 環狀管壁（34)上方複數之流通孔（341)進入於該第四反應流道（39) 内，最後，往下由該出口（27)送出供使用；而，經由以上所述於液體 (L+03)進入本創作反應槽（20)内流動之動線（如第三圖上所繪製之箭 頭方向所示），可以很清楚的得知，當液體仏+03)通過複數、孔徑袓當 細小之流通孔（311)(321)(331)(341)時，可使液體產生氣泡化、液面 薄膜化的現象，因此得以增加液體(L)與氣體(〇3)接觸面積，則液體仏） 與氣體(03)之反應增加，所以液體(L+〇3)内氣體(〇3)之含量比率得以 提昇；而，液體(L)流動時，係由較寬大之反應流道(35)〜（39)縮小變 成由孔徑約（6mm~12mm)之流通孔流出，再進入較寬大之反應流道，如 此反覆的由大變小、再由小變大，使液體流速產生變化，加速的液體 流速可產生衝擊動力，使液體⑹與氣體(〇3)可以充份混合，而層層迴 流的設計，則可使氣體(03)產生滯留效果，拉長液體江)與氣體(〇3) 的混合時間，增加氣液混合之溶解，以為本創作之創作特點，而能 提高殺菌、消毒、除臭之各種功效，達成本創作預期之創作目的。 M284436 第五_本_另-實施例之示_，_反應槽(2G)槽體(23) 之外端，以螺旋繞設之方式設置有一循環冷卻管（28)，冷卻管（28) 内通以水流，可控制反應槽（2〇)溫度維持於某一低溫狀態，避免反應 槽（20)因日曬、雨淋以及反應作用時間過長，而產生溫度變化差異太 大，影響氣液混合作用時之溶解率及其穩定性；又，該反應槽（2〇)上 更設置有一洩壓閥（29)，以控制槽體(23)内之壓力保持於一定範圍之 穩定狀態，確保反應槽（20)使用之安全性。 鲁 【圖式簡單說明】 第一圖係習用一種臭氧與液體混合器之結構剖視示意圖。 第二圖係本創作一較佳實施例反應槽之立體外觀示意圖。 第三圖係第二圖反應槽之縱向剖視示意圖。 第四圖係第二圖反應槽之A-A剖視示意圖。 第五圖係本創作另一較佳實施例反應槽之外觀平面示意圖。 【符號簡單說明】 習用途號： 混合器（1) 本創作圖號： 氣液混合反應槽（20) 入口（25) 循環冷卻管(28) 環狀管壁(30)〜(34) 反應流道(35)〜(39) 液體(U 臭氧(03) 槽體(23) 出口（27) 洩壓閥（29) 流通孔(311) (321) (331)(341) 7M284436 VIII. New description: [New technical field] This is a kind of reaction tank that can mix (4) with liquid, especially a physical method to increase the gas (ozone) content in liquid (tap water). A gas-liquid reaction tank with a higher dissolution ratio of gas-liquid mixture and enhanced sterilization and disinfection. [Prior Art] It is known in the past that 'the ozone generator can provide the ozone gas, and the ozone can eliminate the bacteria to achieve the secret and deodorization effect. The creator of this case has invented a mixer (1). (Refer to the first 囷), let the liquid α) (that is, generally from I water) and the ozone (10) fed by the ozone generator (not shown) pass through the mixer (1) simultaneously. (6) contains ozone (10), which can be used for cleaning, disinfecting, removing pesticides and odors when cleaning clothes and fruits and vegetables; however, these ozone generators must consume high energy because of the special 'production of ozone. Ozone is not easy to obtain, and how can it be required to contain a higher concentration of ozone in the liquid to enhance its sterilization and disinfection, and how to cope with the needs of ordinary people, long-term, large-scale use. [New content] In view of the fact that in order to increase the concentration of ozone in the liquid, that is, to increase the speed and efficacy of sterilization, the key is the time when the liquid reacts with ozone, which is developed by a physical method to increase the bubble of the liquid. The contact area with ozone gas, 卩 and the use of layer reflow design, reduce the thorns, increase the liquid odor and the combination of the time and time can be high gas-liquid mixing speed and dissolution rate. m The creation-type gas-liquid mixed reaction tank is provided with “population and output σ”, which is for the liquid of M284436 which already contains ozone, and the outlet is for the liquid output after entering the reaction tank; There are several layers of reaction channels, each of which is provided with a number of small and small flow holes in the staggered position to circulate 'to increase the contact area of the liquid bubble with the ozone gas'. The layer reflow design can generate a stagnant effect. Increasing the mixing time of the liquid and the ozone gas, thereby increasing the speed of gas-liquid mixing and the dissolution rate, and improving the bactericidal effect. [Embodiment] A gas-liquid mixing reaction tank (20) is created. Referring to the second and third figures, φ is a circular tubular body (23) having an inlet (25) and a An outlet (27) for entering a liquid (L) (generally tap water) containing ozone (〇3), that is, passing a liquid (generally tap water) through a mixer (as shown in the first figure) After being shown, the liquid (L+03) containing ozone (03) in the liquid (L) enters the tank (23) and reacts; the outlet (27) is supplied to the reaction tank of the present invention (20). After the action, the liquid (force) containing high concentration of ozone is output; and the groove (23) of the creation reaction tank (20), please refer to the third figure and the fourth # _, by means of - The layer-to-layer annular tube walls (10) to (34) are partitioned to form a plurality of counter-links (35) to (39) as passages for liquid circulation; and the inlet (25) is provided on the first layer ( Above the annular tube wall (10) of the outermost circle, and then under the annular tube wall (8) of the second layer, a plurality of holes having a relatively small aperture (approximately between 6 mm and 12 mm) and a third layer are provided. Tube wall (10) Wei (321), sequentially below the annular tube wall (10) of the fourth layer, above the fifth annular tube wall (10), with the layer above, and then below the lower-warm Holes (331), (341), and the outlet (27) is disposed below the reaction channel (10) of the last-®, staggered at the position where the ring 5 M284436 pipe wall (34) is provided with the flow hole (341) above. . With the above design, the inlet (25) above the creation reaction tank (20) enters the liquid (L+03) containing a lower concentration of ozone (〇3) in the tank body (23), first through the first The reaction channel (35) goes down and enters the second reaction channel (35) through a plurality of flow holes (311) disposed under the annular tube wall (31) of the second layer, and then the second The reaction channel (36) is upwardly inserted into the second reaction channel (37) through a plurality of flow holes (321) disposed above the third layer of the annular tube wall (32), and is disposed through the main channel The plurality of flow holes (331) of the annular pipe wall (33) of the third layer are inserted into the fourth reaction flow path (38) upward, and are disposed above the fourth annular pipe wall (34). The flow hole (341) enters the fourth reaction flow path (39), and finally, is sent out from the outlet (27) for use; and, through the above, the liquid (L+03) enters the creation reaction tank. (20) The moving line of the inner flow (as indicated by the direction of the arrow drawn on the third figure), it can be clearly seen that when the liquid 仏+03) passes through the complex, the aperture is a small flow hole (311) ( 321 (331) (341), the liquid can be bubbled and the liquid surface is thinned, so that the contact area between the liquid (L) and the gas (〇3) is increased, and the liquid 仏) reacts with the gas (03). Increasing, so the ratio of the content of the gas (〇3) in the liquid (L+〇3) is increased; and when the liquid (L) flows, it is reduced by the wider reaction channels (35) to (39) to become the pore diameter. The flow hole of (6mm~12mm) flows out, and then enters the wider reaction flow channel, so that the repeated change from large to small, then from small to large, the liquid flow rate changes, the accelerated liquid flow rate can generate impact power, make the liquid (6) It can be mixed with gas (〇3), and the layer reflow design can make the gas (03) have a retention effect, lengthen the mixing time of the liquid river and the gas (〇3), and increase the gas-liquid mixing. Dissolving, in order to create the characteristics of the creation, and can improve the various functions of sterilization, disinfection, deodorization, to achieve the creative purpose of this creation. M284436 Fifth_本_其他_Example _,_Reaction tank (2G) tank (23) The outer end is provided with a circulating cooling pipe (28) in a spiral winding manner, and the cooling pipe (28) Through the water flow, the temperature of the reaction tank (2〇) can be controlled to maintain a certain low temperature state, and the reaction tank (20) is prevented from being exposed to the sun, rain and reaction time for too long, and the temperature difference is too large, affecting the gas and liquid. The dissolution rate and stability of the mixing action; further, a pressure relief valve (29) is further disposed on the reaction tank (2〇) to control the pressure in the tank body (23) to maintain a stable range within a certain range, thereby ensuring a stable state. The safety of the reaction tank (20) is used. Lu [Simple diagram of the diagram] The first diagram is a schematic cross-sectional view of a structure of an ozone and liquid mixer. The second drawing is a schematic perspective view of a reaction tank of a preferred embodiment of the present invention. The third figure is a longitudinal cross-sectional view of the reaction tank of the second figure. The fourth figure is a schematic cross-sectional view of the A-A of the reaction tank of the second figure. The fifth drawing is a schematic plan view showing the appearance of a reaction tank according to another preferred embodiment of the present invention. [Simplified symbol] Application No.: Mixer (1) This creation number: gas-liquid mixed reaction tank (20) inlet (25) circulating cooling tube (28) annular wall (30) ~ (34) reaction flow Road (35) ~ (39) Liquid (U Ozone (03) Tank (23) Outlet (27) Pressure Relief Valve (29) Flow Hole (311) (321) (331) (341) 7