TWI361111B - - Google Patents
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- TWI361111B TWI361111B TW098128660A TW98128660A TWI361111B TW I361111 B TWI361111 B TW I361111B TW 098128660 A TW098128660 A TW 098128660A TW 98128660 A TW98128660 A TW 98128660A TW I361111 B TWI361111 B TW I361111B
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61H—PHYSICAL THERAPY APPARATUS, e.g. DEVICES FOR LOCATING OR STIMULATING REFLEX POINTS IN THE BODY; ARTIFICIAL RESPIRATION; MASSAGE; BATHING DEVICES FOR SPECIAL THERAPEUTIC OR HYGIENIC PURPOSES OR SPECIFIC PARTS OF THE BODY
- A61H33/00—Bathing devices for special therapeutic or hygienic purposes
- A61H33/02—Bathing devices for use with gas-containing liquid, or liquid in which gas is led or generated, e.g. carbon dioxide baths
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47K—SANITARY EQUIPMENT NOT OTHERWISE PROVIDED FOR; TOILET ACCESSORIES
- A47K3/00—Baths; Douches; Appurtenances therefor
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61H—PHYSICAL THERAPY APPARATUS, e.g. DEVICES FOR LOCATING OR STIMULATING REFLEX POINTS IN THE BODY; ARTIFICIAL RESPIRATION; MASSAGE; BATHING DEVICES FOR SPECIAL THERAPEUTIC OR HYGIENIC PURPOSES OR SPECIFIC PARTS OF THE BODY
- A61H33/00—Bathing devices for special therapeutic or hygienic purposes
- A61H33/60—Components specifically designed for the therapeutic baths of groups A61H33/00
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
- B01F23/213—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids
- B01F23/2132—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids using nozzles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
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Description
1361111 、發明說明: 【發明所屬之技術領域】 本發明係關於使用於產生微細氣泡之熱水的生 成之空氣溶解水生成裝置。詳言之,本發明係關於 空氣溶料生絲置,其構成為製成空氣溶解於水 之氣體溶解水,接著自氣體溶解水製成含有微细氣 泡之熱^又,本發明係關於具備空氣溶解水生成 裝置之浴槽。 【先前技術】 4 ^本公開公報日本特開2 Q〇 7-3 i 3 4 6 j = _往的空氣溶解水生成裝置。以往的空氣 :著軸=裳置具備槽與泵。槽具圓筒形狀,具有 :::方向之長度。該槽相對於水平方直 向而將軸方向呈傾斜配置罝方 向之第二端更高位置的第一有位於較軸方 口、液邮、鸲。槽具備液體流入 液祖流出口、及空氣流出口。 成於槽外周面以位;液·入口係形 係形—s 的位置。液體流出口 你化成於槽外周面以位於 體流入口與液體流出口係朝向夂,的位置。液 形成於槽之外周面以位於工虱流出口係 氣流入口係朝0 θ第一端侧的位置。空 邱钥句上方。泵盥. 由液體流入口盥玄、$、帛…,,&源連接。泵經 在以往之料“至果内。- 工就讀水生成裝置中,I係經由液 3 =口’在槽内喷出水或混合有氣體之水。噴出 製内的空氣混合。結果氣體溶解,且 =有氣泡之水。溶解有氣趙之水,係所謂的氣 :::水。該氣趙溶解水流至槽下方。 2體溶解水經由液體流出σ,自槽輸送至浴槽 气、方面在流至槽下方的氣體溶解水殘留大型 氣,包時k在槽内再度分離成液體與氣體。又,自 泵所輸送之液體在屬於混合氣體之水時,在槽内盘 水一起持續供給空H。兮处名 、 釋放口釋出。 “係自設置於槽的氣體 但是在以往之空氣溶解水生成裝置中,會有大 多未溶解氣體易於滯留於槽中的問題。槽内未溶解 氣體難以溶解於槽内之水。因此’以往之空氣溶解 ,生成裝置會有難以高效率製成氣體溶解水之問 題。為了將该未溶解氣體減少,有必要將滯留於槽 中1氣體與水之接觸時間變長’然而欲使該時間^ 長日才,會有用以使之接觸之路徑變長,裝置變成大 型化的問題。 又’將空氣溶解水生成裝置與浴槽連接,藉由 泵將儲存於洛槽之水供給於空氣溶解水生成裝置, 藉由將自液體流出口流出之空氣溶解水回至浴槽使 之循裱,使微細氣泡自空氣溶解水產生,構成附有 二氣溶解水生成裝置之浴槽。在此時,.於空氣溶解 水中混入大徑的氣泡時,在微細氣泡中亦混入了大 徑的氣泡,會有造成浴槽水品質降低的問題。 【發明内容】 本發明係為解決上述問題而完成者。本發明之 目的係提供一種空氣溶解水生成裝置,其構成為以 高效率生成氣體溶解水,且使未溶解氣泡之流出減 少〇 為解決上述課題,本發明之空氣溶解水生成裝 置具備:一槽,其具備液體流入口及液體流出口; 一喷出路徑,其連接該液體流入口,同時設置成.可 連接於水供給源,流經該喷出路徑之水係構成為喷 出至該槽,藉此在該槽混合水與空氣,製成氣體溶 解於該水之氣體溶解水,該槽具備隔壁,該隔壁係 將該槽内部劃分成混合室與分離室,該隔壁係自該 槽之底拉離而配置,藉此形成連通該混合室與該分 離室之連通路,該液體流入口係設置於該混合室, 該液體流出口係設置於.該分離室,該分離室係自該 混合室經由該連通路接受含有氣泡之氣體溶解水, 分離該氣體溶解水與氣泡,經分離之該氣體溶解水 自該液體流出口供應至外部,經分離之氣泡與滯留 於該分離室上部之氣體一起滯留於分離室上部,進 而具備回流管路,用以連通該分離室與該喷出路 徑,將滯留於該分離室上部之氣體輸送至該喷出路 在此情形可以高效率生成氣體溶解水。 宜為在該分離室之上端部形成空氣流出口,該 回流管路之一端連接該空氣流出口。 宜為在該混合室之下端部形成空氣流入口,該 回流管路之一端連接該空氣流入口。 該喷出路徑係形成空氣流入口,該回流管路之 一端連接該空氣流入口。 宜為該噴出路徑具備喷射器與管路,該喷射器 具備第一端與第二端,該第一端與該管路之第一端 連結,該第二端連接槽,在該喷射器之該第一端形 成空氣流入口,在該喷射器及該管路内部具備流 路,該喷射器之該第一端流路之剖面積形成較該管 路之該第一端流路之剖面積更大,該回流管路之一 端連接該空氣流入口。 在此情形,可將以回流管路輸送至喷出路徑的 空氣效率良好的溶解於流經喷出路徑之水。 接著,該空氣流入口宜為設置於該喷射器。接 著,空氣流入口宜為設置於喷射器之第一端。 在該分離室之上端宜為設置空氣釋放閥。 宜構成為將混合有空氣之該水自該喷出路徑噴 1361111 出至該混合室,自該空氣釋放閥所釋放空氣之每單 位時間的體積宜為設定於自該喷出路徑喷出之水所 含該空氣每單位時間體積的2 0 %以上。 宜為該分離室係以擋板劃分成第一副分離室與 第二副分離室,該擋板係形成為,該擋板之上端自 該槽上面拉離,藉此以形成連通第一副分離室與第 二副分離室之連通口,將自該混合室所輸送之含有 氣泡的氣體溶解水經由該第一副分離室導引至該第 二副分離室’該液體流出口形成於該弟二副分離室 之下端。 又宜為使液體流出口設置於第二副分離室之底 部,且設定氣液分離槽之剖面積,使流經第二副'分 離室之液體流速相對於自液體流出口流出外部之液 體流速,為1/5以下。 在此情形,在含有氣泡之氣體溶解水經由擋板 上端自第一副分離室流至第二副分離室時,可使氣 泡以高效率自氣體溶解水分離。 宜為上述槽具有界定該分離室上端内壁之上 壁,該第二副分離室之上端内壁係以傾斜壁界定, 該傾斜壁係自該第一副分離室上端内壁連續朝下方 傾斜,該回流管路連接該第一副分離室上方之該槽 上壁。 7 1361111 在此情形可以高比率自回流管路輸送空 出路徑。 g 空氣溶解水生成裳置宜進一步具備空氣釋放 …亥空氣釋放閥係由内部具備浮標之汽缸筒(b :r r e 1 )所構成,該空氣釋放閥具有較該第二 ::離室上方之該槽上壁更位於下方位置的下端, 5亥A缸筒宜為使開口形成於其側面之下端部。 宜為該擋板及該隔壁具有互為相向之一面,該 :板或该隔壁之任一者係朝向該擋板或該隔壁之另 方而突出,形成在該槽之高度方向延伸的導板。 之二經第,離室之含有氣泡 水在弟-副分離t之上部效率良好的分 離成軋泡與氣體溶解水。 宜為在該擋板之上端中央具有延伸板,其係朝 向该槽上面而延伸。 在:情形,可將自第一副分離室流至第二副分 至之3有_之氣體溶解水效率良好的分離 泡與氣體溶解水。 ” 宜為在該分離室設置整流板,其係自該分離室 之官SI!:下方延伸’該整流板形成於與該延伸板 之莧方向父差的方向。 在此情形,可自從第二副分離室之上部流至下 8 1361111 部之含有氣泡之氣體溶解水效率良好的分離氣泡與 氣體溶解水。 空氣溶解水生成裝置係安裝於浴槽,該空氣溶 解水生成裝置係設置於循環流路,該循環流路係自 一端部之吸進口吸進浴槽内熱水且自另一端之液體 排放口喷出至浴槽内,藉由自該液體流出口所供應 之氣體溶解水,自液體排放口噴出微細氣泡於浴槽 内。 又,空氣溶解水生成裝置宜配置於浴室。該浴 室宜具備:一浴槽;一洗蘇場,其與該洛槽鄰:接;·而 設;一外蓋,用以覆蓋該浴槽之洗滌場側之面,藉 此,在該外蓋與該浴槽之間形成收納空間,該浴槽 係使該空氣溶解水生成裝置設置於循環流路,該循 環流路自一端部之吸進口吸進浴槽内熱水且自另一 端液體排放口喷出至浴槽内,藉由自該液體流出口 所供應之氣體溶解水,自液體排放口喷出微細氣泡 至浴槽内,該外蓋係定義洗滌場與浴槽之境界,該 空氣溶解水生成裝置配置於該收納空間,在該空氣 溶解水生成裝置與該外蓋之間配置防音材料。 【實施方式】 第一圖係顯示本發明實施形態之空氣溶解水生 成裝置之基本構造的立體圖。如第一圖至第五圖所 9 1361111 示,空氣溶解水生成裝置丄具備業已密閉之槽2 及回:管路12。在槽2之底具備“流入 4,、液體流出口 8。槽2上端設有空氣流出口丄 3。液體流入口 4係經由於側面形成有空氣流入口 而安裝有水供給管路5。:體流 口 8、&由官路9設置用以輸送後述氣體溶解水。 回流管路12具有與空氣流出口13連接之黛一 :、和與空氣流入口 i 4連接之第二端。泵7係經 由噴射器17及水供給管路5與槽2相連通 ^與圖未顯示出之水供給源連接。泵7經由水供給 :路5及噴射器!7將水供給源内之水喷出至栌2 。或者泵7經由水供給管路5及喷射器17‘業 =混合外部空氣的水供給源内之水噴出至版 中:因此’泵7係將具有預定水壓的水喷出至槽2 第三圖顯示喷射器丄7與水供給管路$之擴大 4面圖。喷射器丄7且備 ’、 7 9 , , 備弟—端1 7 1與第二端i #。:二給管路5亦具備第-端51與第二 二:7之第一端1 7 1與水供給管路5的 接:喷射器17之第二端”2連接 心 ?、給官路5之第二端連接於泵7。喷射 口口 1 7及水供給管路5夂 器”第-端⑺之二部具有流路。喷射 …第一端51之流路剖面積更大。又,喷射器 10 1361111 上:自第一端朝向第二端而漸漸變大。, ^ 7形成有m 口 14,其係位於料^ 17與水供給管路5之連接部的位置。 、。 2空氣轉水生絲以係如下述動作。在 :7起動之前’在槽2中係以空氣充滿。在泵7起 捋’泵7係將水供給源内之水噴出至槽2中 出水於槽内,噴出於槽内之水衝擊槽“ :寺而弹賤。又,泵7由於持續喷出水於槽内,故 水在槽2内積存。積存於槽2内之水與衝擊之 壁等而彈狀水再度相衝擊。再者,17_ 水育出至槽2申,故槽2中之水被自果7輪送而來 之水所攪拌。 藉由此種衝擊,積存於槽2中的氣體與水工工 混合。藉由使空氣與水混合,而使水中含有大型氣 泡。接著,藉由在槽2中將水攪拌以使水中產生^ 斷力。剪斷力係加諸於業已混合於水之大型氣泡。 承受剪斷力之大型氣泡分裂成微細氣泡。藉由將大 型氣泡分裂成微細氣泡,氣體變成易於溶於水。結 果,空氣溶解於水,藉此可製成氣體溶解水。氣體 溶解水經由液體流出口 8被輸送至浴槽等。被輸送 至浴槽的氣體溶解水曝曬於大氣壓。結果自溶=於 氣體溶解水之水中的空氣,產生微細氣泡。該微細 氣泡停留於水中。如此一來,含有微細氣泡之水被 1361111 供應至浴槽等。一方面,在槽2中未溶解於水之空 氣’成為氣泡浮出於槽2上方而被分離,該氣泡與 滞留於槽上部之氣體一起滯留著。 滯留於槽上部之空氣經由回流管路1 2,被輸 送至喷射器1 7。詳言之,在空氣溶解水生成裝置 1之運作中,泵7係經由水供給管路5及噴射器丄 7,經由液體流入口 4持續供給水於槽2。自泵γ ^過喷射器1 7被輸送至槽2之水進行槽2内加 壓。因此,空氣流出口 1 3之壓力較空氣流入口工 4之壓力更大。藉此在空氣流出口 1 3與空氣流入 '1 4之間產生壓力差。該壓力差係將滯留於槽2 上部之空氣料喊卜被吸進回流管路丄 2之空氣經由空氣流出口 1.3被輸送至噴射器工7 因此在空氣溶解水生成裝置丄 氣經由回流管路12及嘴射器”,再次 曰2中之液體進行循環。 於液體之空氣,再 A為乳泡“合 以氣泡輪送至嗔==液體’藉此再次 中係與液體6-起,再次喷出於槽 液體6。因此^17内之空氣成為氣泡混合於 空氣滯留之情形:6中之氣泡相較於在槽上方以 成為易於溶解於液體6。因此可 12 1361111 將氣體以高效率溶解於液體6。 在此,氣體的溶解速度係以下述式表示。 CV=KL * a .(C*-〇 C v :溶解速度 K L :總括物質移動係數 a ·接觸面積1361111, EMBODIMENT OF THE INVENTION: TECHNICAL FIELD The present invention relates to an air-dissolved water generating apparatus for producing hot water for generating fine bubbles. In particular, the present invention relates to an air-soluble raw material, which is configured to be a gas-dissolved water in which air is dissolved in water, and then to form a heat containing fine bubbles from the gas-dissolved water. The bath of the water generating device. [Prior Art] 4 ^ This publication discloses an air-dissolved water generating device in Japanese Patent Application No. 2 Q〇 7-3 i 3 4 6 j = _. The air in the past: the shaft = the slot with the pump. The trough has a cylindrical shape with a length of ::: direction. The groove is inclined with respect to the horizontal direction, and the axial direction is inclined. The first position of the second end of the second direction is located at the lower axis, liquid mail, and raft. The tank has a liquid inflow liquid progenitor outlet and an air flow outlet. It is placed in the outer peripheral surface of the groove; the position of the liquid/inlet system is the shape of the s. The liquid outflow port is formed in the outer peripheral surface of the tank so that the body flow inlet and the liquid outflow port are facing the crucible. The liquid is formed on the outer peripheral surface of the tank so as to be located at the first end side of the 0 θ flow inlet of the work outlet. Empty Qiu key sentence above. Pump 盥. Connected by liquid inflow, $, $, 帛..., & source. The pump is used in the previous material "to the fruit. - In the working water generating device, I is sprayed with water or mixed with water through the liquid 3 = port. The air in the spray system is mixed. As a result, the gas is dissolved. And = water with bubbles. Dissolved water of Zhao Zhao, the so-called gas::: water. The gas dissolved water flows to the bottom of the tank. 2 body dissolved water flows out through the liquid σ, from the tank to the bath gas, in the flow The gas dissolved in the gas below the tank remains large gas, and the package k is separated into liquid and gas again in the tank. Further, when the liquid delivered from the pump is in the water belonging to the mixed gas, the water in the tank is continuously supplied with the air H. The name and the release port are released. "The gas is set in the tank. However, in the conventional air-dissolved water generator, there is a problem that most of the undissolved gas tends to stay in the tank. The undissolved gas in the tank is difficult to dissolve in the water in the tank. Therefore, the conventional air dissolving and generating device has a problem that it is difficult to efficiently produce a gas dissolved water. In order to reduce the amount of undissolved gas, it is necessary to increase the contact time between the gas and the water in the tank. However, in order to make the time longer, the path for bringing the contact becomes longer, and the apparatus becomes larger. The problem. Further, 'the air-dissolved water generating device is connected to the bath, and the water stored in the tank is supplied to the air-dissolved water generating device by the pump, and the air discharged from the liquid outlet is dissolved in the bath to be circulated, The fine bubbles are generated from the air-dissolved water to form a bath with a two-gas dissolved water generating device. At this time, when bubbles having a large diameter are mixed in the air-dissolved water, bubbles having a large diameter are also mixed in the fine bubbles, which may cause a problem that the quality of the bath water is lowered. SUMMARY OF THE INVENTION The present invention has been made to solve the above problems. An object of the present invention is to provide an air-dissolved water generating apparatus which is configured to generate gas-dissolved water with high efficiency and reduce outflow of undissolved air bubbles. To solve the above problems, the air-dissolved water generating apparatus of the present invention comprises: a tank a liquid inflow port and a liquid outflow port; a discharge path connected to the liquid inflow port and configured to be connectable to the water supply source, and the water system flowing through the ejection path is configured to be ejected to the trough Thereby, water and air are mixed in the tank to form a gas dissolved water in which the gas is dissolved, and the tank is provided with a partition wall, and the partition wall divides the inside of the tank into a mixing chamber and a separation chamber, and the partition wall is from the tank a bottom portion is disposed to form a communication path connecting the mixing chamber and the separation chamber, the liquid inflow port is disposed in the mixing chamber, and the liquid outflow port is disposed in the separation chamber, the separation chamber is from the The mixing chamber receives the dissolved water containing the bubbles through the communication path, and separates the dissolved water and the bubbles of the gas, and the separated dissolved water is supplied to the outside from the liquid outlet, and is divided into The bubble is retained in the upper portion of the separation chamber together with the gas remaining in the upper portion of the separation chamber, and further includes a return line for communicating the separation chamber and the discharge path, and conveying the gas retained in the upper portion of the separation chamber to the discharge. In this case, the road can efficiently generate gas dissolved water. Preferably, an air flow outlet is formed at an upper end of the separation chamber, and one end of the return line is connected to the air flow outlet. Preferably, an air flow inlet is formed at the lower end of the mixing chamber, and one end of the return line is connected to the air flow inlet. The discharge path forms an air flow inlet, and one end of the return line is connected to the air flow inlet. Preferably, the ejection path is provided with an ejector and a tube, the ejector having a first end and a second end, the first end being coupled to the first end of the tube, the second end being coupled to the slot, at the ejector The first end forms an air flow inlet, and the flow path is provided inside the injector and the pipeline, and a cross-sectional area of the first end flow path of the injector forms a sectional area of the first end flow path of the pipeline Larger, one end of the return line is connected to the air flow inlet. In this case, the air which is sent to the discharge path by the return line can be efficiently dissolved in the water flowing through the discharge path. Next, the air flow inlet is preferably provided to the injector. Next, the air flow inlet is preferably disposed at the first end of the injector. An air release valve is preferably provided at the upper end of the separation chamber. Preferably, the water mixed with air is discharged from the discharge path 1361111 to the mixing chamber, and the volume per unit time of the air released from the air release valve is preferably set to be discharged from the discharge path. The air contained is more than 20% of the volume per unit time. Preferably, the separation chamber is divided into a first sub-separation chamber and a second sub-separation chamber by a baffle, and the baffle is formed such that an upper end of the baffle is pulled away from the groove, thereby forming a first pair of communication a communication port between the separation chamber and the second sub-separation chamber, and the bubble-containing gas-dissolved water transported from the mixing chamber is guided to the second sub-separation chamber through the first sub-separation chamber. The second side of the second separation room. Further, it is preferable to set the liquid outflow port at the bottom of the second sub-separation chamber, and set the cross-sectional area of the gas-liquid separation tank so that the liquid flow rate flowing through the second sub-separation chamber is relative to the liquid flow rate flowing out from the liquid outflow port to the outside. , for 1/5 or less. In this case, when the dissolved water containing gas bubbles flows from the first sub-separation chamber to the second sub-separation chamber through the upper end of the baffle, the bubble can be separated from the gas-dissolved water with high efficiency. Preferably, the groove has an upper wall defining an inner wall of the upper end of the separation chamber, and an inner wall of the upper end of the second sub-separation chamber is defined by an inclined wall which is continuously inclined downward from an inner wall of the upper end of the first sub-separation chamber, the reflow A pipe is connected to the upper wall of the tank above the first secondary separation chamber. 7 1361111 In this case, the empty path can be delivered from the return line at a high ratio. g Air dissolved water generation should be further equipped with air release... The air release valve is composed of a cylinder tube (b:rre 1 ) with a buoy inside, and the air release valve has a second:: above the chamber The upper wall of the groove is located at the lower end of the lower position, and the 5A cylinder is preferably formed such that the opening is formed at the lower end of the side. Preferably, the baffle and the partition wall have opposite sides of each other, and the plate or the partition wall protrudes toward the baffle or the other side of the partition wall to form a guide plate extending in a height direction of the groove . In the second, the bubble contained in the chamber is separated from the bubble-dissolved water by the gas in the upper part of the sub-separation t. Preferably, there is an extension plate at the center of the upper end of the baffle which extends toward the groove. In the case, it is possible to flow from the first sub-separation chamber to the second sub-divided to 3 gas-dissolved water-dissolving water and gas-dissolving water. It is preferable to provide a rectifying plate in the separating chamber, which is extended from the official SI!: lower portion of the separating chamber. The rectifying plate is formed in a direction opposite to the parent direction of the extending plate. In this case, since the second The bubble in the upper portion of the sub-separation chamber flows to the lower portion of the air, and the gas-dissolved water is dissolved in the air. The air-dissolved water generating device is installed in the bath, and the air-dissolved water generating device is disposed in the circulation flow path. The circulating flow path is sucked into the bath from the suction inlet of the one end portion and ejected from the liquid discharge port at the other end into the bath, and the gas supplied from the liquid outflow port dissolves the water from the liquid discharge port. The fine air bubbles are sprayed in the bath. Further, the air-dissolved water generating device should be disposed in the bathroom. The bathroom preferably has: a bath; a washing field, which is adjacent to the Luo slot; and is provided; Covering the surface of the washing tank side of the bath, a storage space is formed between the outer lid and the bath, and the bath is provided in the circulation flow path by the air dissolved water generating device. The suction inlet of the part sucks into the hot water in the bath and is ejected from the liquid discharge port at the other end into the bath, and the fine air bubbles are ejected from the liquid discharge port into the bath by dissolving the water supplied from the liquid outflow port. The outer cover defines a boundary between the washing field and the bath, and the air-dissolved water generating device is disposed in the storage space, and a soundproof material is disposed between the air-dissolved water generating device and the outer cover. A perspective view of a basic structure of an air-dissolved water generating apparatus according to an embodiment of the present invention. As shown in the first to fifth figures 9 1361111, the air-dissolved water generating apparatus 丄 has a closed tank 2 and a return line 12 in the tank 2 The bottom has "inflow 4, liquid outlet 8". An air outlet port 3 is provided at the upper end of the tank 2. The liquid inflow port 4 is provided with a water supply line 5 via an air inflow port formed on the side surface. The body fluid port 8, & is provided by the official road 9 for conveying the gas dissolved water described later. The return line 12 has a first connection to the air flow outlet 13 and a second end connected to the air flow inlet i4. The pump 7 is connected to the tank 2 via the ejector 17 and the water supply line 5, and is connected to a water supply source not shown. Pump 7 is supplied via water: way 5 and ejector! 7 Spout water from the water supply to 栌2. Or the pump 7 is ejected into the plate via the water supply line 5 and the ejector 17' industry = water in the water supply source of the mixed external air: therefore, the pump 7 squirts water having a predetermined water pressure to the tank 2 An enlarged four-sided view of the injector 丄7 and the water supply line $ is shown. The injector 丄7 is provided with ', 7 9 ', and the second side is the first end i #1. The second supply line 5 also has a first end 51 and a second second: 7 first end 17 1 and the water supply line 5: the second end of the injector 17 "2" connects the heart?, to the official road The second end of 5 is connected to the pump 7. The injection port 17 and the water supply line 5 have two flow paths of the first end (7). The cross-sectional area of the flow path of the first end 51 is larger. Further, the ejector 10 1361111 is gradually enlarged from the first end toward the second end. , ^ 7 is formed with a m port 14, which is located at the position of the connection portion between the material 17 and the water supply line 5. ,. 2 Air-to-water raw silk is operated as follows. Before the start of :7, the tank 2 is filled with air. In the pump 7, the pump 7 is used to spray water from the water supply source into the tank 2 to discharge water into the tank, and the water sprayed into the tank impinges on the tank ": the temple is impeached. Further, the pump 7 continues to spray water. In the tank, water accumulates in the tank 2. The water accumulated in the tank 2 collides with the wall of the impact and the bullet-like water again. Further, 17_ water is bred to the tank 2, so the water in the tank 2 is The water is stirred by the 7 rounds of water. With this impact, the gas accumulated in the tank 2 is mixed with the water worker. By mixing the air with the water, the water contains large bubbles. The water is agitated in the tank 2 to cause a breaking force in the water. The shearing force is applied to the large bubbles which have been mixed with water. The large bubbles which are subjected to the shearing force are split into fine bubbles. The bubbles become gas-soluble and easily dissolved in water. As a result, the air is dissolved in water, whereby the gas-dissolved water can be produced. The gas-dissolved water is sent to the bath or the like via the liquid outflow port 8. The dissolved water which is sent to the bath is exposed to atmospheric pressure. The result is autolysis = air in the water in which the gas dissolves water, producing micro The fine bubbles stay in the water. In this way, the water containing the fine bubbles is supplied to the bath or the like by 1361111. On the other hand, the air which is not dissolved in the water in the tank 2 becomes separated from the bubble 2 and is separated. The air bubbles are retained together with the gas remaining in the upper portion of the tank. The air remaining in the upper portion of the tank is sent to the injector 17 via the return line 12. In detail, in the operation of the air-dissolved water generating device 1, The pump 7 continuously supplies water to the tank 2 via the water supply line 5 and the ejector bowl 7, and the water that has been transported from the pump γ ^ over-injector 17 to the tank 2 is pressurized in the tank 2. Therefore, the pressure of the air flow outlet 13 is greater than the pressure of the air flow inlet 4, whereby a pressure difference is generated between the air flow outlet 13 and the air flow '14. The pressure difference will remain in the upper portion of the tank 2. The air is sucked into the return line 丄2 and the air is sent to the ejector 7 via the air outflow port 1.3. Therefore, in the air dissolved water generating device, the helium gas passes through the return line 12 and the mouthpiece", again 曰2 The liquid in the circulation is circulated. In the air of the liquid, then A is the emulsion "combined with the bubble wheel to 嗔 = = liquid", thereby re-spraying from the liquid 6 again, and then the air in the groove 17 is bubbled. In the case of air retention: the bubble in 6 is easier to dissolve in the liquid 6 than in the groove. Therefore, the gas can be dissolved in the liquid 6 with high efficiency at 12 1361111. Here, the dissolution rate of the gas is expressed by the following formula CV=KL * a .(C*-〇C v : dissolution rate KL : total material movement coefficient a · contact area
C * :飽和溶解氣體濃度 C:溶解氣體濃度 久1、邛C * : Saturated dissolved gas concentration C: Dissolved gas concentration Long 1, 邛
Mu 谷解迷度係以與液體之接鈣^ 積,和與氣體濃度梯度之乘積來計算接= 接觸面積a變大,溶解速度“變大。妾者、奢 接著,本發明空氣溶解The Mu Valley solution is calculated by multiplying the calcium product with the liquid and the product of the gas concentration gradient. The contact area a becomes larger, and the dissolution rate becomes larger. The latter is extravagant.
相對於滿姊只,L 〜玍成展置1,空氣係 因:Γ· 氣流入口14以氣泡輪送。 口此相#乂於在槽上方以空氣滯 體6之接觸面積大。心=㈣’空氣與液 。 於紐時間可將空氣溶解於 液體6。亦即,為使㈣溶解效率提高,並血需延 J液㈣與氣體的接觸時間。因此,不需加大液體 之路徑’即可提高氣體之溶解效率。因此可謀求 虞置小型化。又滞留於槽2上部的空氣係經由喷射 為1 7被輸送至槽2下端。因.此難以攪亂槽2中水 之液面。藉此可抑制大型氣泡流出。 又’空氣溶解水生成裝置1具備回流管路1 2。因此在滯留於槽上部的氣體1 8消失為止,可 經由回流管路1 2持續氣體之循環。藉此,空氣溶 解水生成裝置1在槽2内部經長時間可將空氣持續 溶解於液體。又,回流管路i 2因係使滯留於槽2 上部之氣體在槽2下端循環’故可以高效率進行液 體與氣體之攪拌。 又,空氣流入口 1 4係設置於噴射器丄7,藉 此空氣流入口 1 4係位於槽2之底部3。因此在槽 ,中使液體移動之氣體丄8可長時間與流體6持^ 接觸。因此,可進一步將氣體以高效率溶解於液體。 又,在空氣溶解水生成裝置丄巾空氣流入口 1 4係形成於喷射η 7 ’其係位於在構成喷出路徑 之水供給管路5射射器i 7之接合部分i 6管和 :急遽擴大的部分之位置。因此,自泵7所輸送之: ^通過水供給管路5,接著通過噴射器丄7最 =2中。在此,噴射器17之第一端流路的剖 ,係設U較水供給管路5第—端流路之剖面積 此,流經水供給管路5之液體流速,相較 射器17之液體流速更快。藉由該流速之 ’與在空氣流人π ! 4急遽擴A的部分 内產生渦流。該渴流係經過回流管路 2及工仏人口 χ 4將滞留於槽2上端之巧以 1361111 強大吸引壓力吸進。因此藉由該構成,流至氣體工 8的賀射器1 7之量增加。再者,流速之差係在喷 ' 射器1 7中產生剪斷力。該剪斷力係加諸於經由空 .· 氣流入口 1 4所吸進之空氣,藉此剪斷力係將輸送 至噴射器1 7之液體中的氣泡分裂成微細氣泡。含 . 有該微細氣泡之液體被輸送至槽2。亦即槽内氣體 與液體之接觸面積進而增大。再者,由於因流速之 # 差所產生之吸引壓力高,故在回流管路1 2中無灰 塵等的堵塞。亦即並無需將回流管路1 2内徑特別 減小。 此外,在空氣溶解水生成裝置丄中空氣流出口 13附近之壓力P1、與空氣流入口14附近之壓 力P 0的壓力差△P越大,則滯留於槽2上部之处 氣被吸進噴射器1 7之量增大。接著,氣泡與^ 藝 ^接觸面積越大,氣體之相對於液體的溶解效率變 局。因此在本實施形態中噴射器1 7第一端之流路 面積係,定為較水供給管路5第—端之流路面積更 大。^是藉由泵等,亦可強制地使滯留於槽2上部 :空氣循環。在此情形,係將空氣流入口形成於槽 之底接著設置泵,其構成係經由回流管路1 • 將空氣輸送至空氣流入口。 又,在本實施形態中液體流入口 4係形成於槽 之底。但是如第四圖所示,宜為設置液體流入口 4於槽2側壁。在此愔p 的位置以外之構成係與第’:體流入口4之槽2中 溶解水生成裝置“目=第二圖所不之空氣 輸送至喷射器17之氣體„形’液體11與被 定為較第-圖及第二的接觸距離τ,係設 中之接觸距離更短。二溶解水生成裝置1 定。此外,該構成可將接觸可適宜設 方向之介丨 ,二虱溶解水生成裝置1高度 二=二又即使空氣流入口 14係設置於 才曰2下部亦可獲得相同效果。 又,在本實施形態中,自 構成噴出路徑之水7所^之水通過 喷出於Γγ 路5與喷射器17形成為 ± 在流經給水管之水的水壓為高 田'1且為不使用泵而將噴出路徑連接於給水管,使 用、这給水管之水的水璧而嘴出於槽2中。在此情 形不需啟動泵的動力。 社此h (實施形態一) 第十-圖係顯示本發明實施形態一之空氣溶解 二成裝置1之立體圖。第五圖係顯示關於本發明 貫施形態-之空氣溶解水生成裝置i的概略圖。此 外’對與顯示第一圖及第二圖之空氣溶解水生成裝 置1的基本構造為相同之構成,賦予相同符號,其' 說明在基本上予以省略。太眘& /、 洎唂奉男、施形態之空氣溶解水 生成裝置1係如第六圖至第十一圖所示,具備槽 16Only L 玍 玍 展 , , , , , , , , , , , , , , , , , , , , , 空气 空气 空气 空气 气流 气流This phase of the mouth is larger than the contact area of the air stagnation 6 above the groove. Heart = (four) 'air and liquid. Air can be dissolved in liquid 6 during the time. That is, in order to improve the dissolution efficiency of (4), the blood needs to extend the contact time of the liquid (4) with the gas. Therefore, the gas dissolution efficiency can be improved without increasing the path of the liquid. Therefore, it is possible to reduce the size of the device. The air remaining in the upper portion of the tank 2 is sent to the lower end of the tank 2 through the injection of 17. This makes it difficult to disturb the level of water in the tank 2. Thereby, large bubbles can be suppressed from flowing out. Further, the air-dissolved water generating device 1 is provided with a return line 1 2 . Therefore, the gas circulation can be continued via the return line 12 2 until the gas 18 remaining in the upper portion of the tank disappears. Thereby, the air-dissolved water generating device 1 can continuously dissolve the air in the liquid inside the tank 2 for a long time. Further, since the return line i 2 circulates the gas remaining in the upper portion of the tank 2 at the lower end of the tank 2, the liquid and the gas can be stirred with high efficiency. Further, the air inflow port 14 is provided in the injector port 7, whereby the air inflow port 14 is located at the bottom 3 of the tank 2. Therefore, the gas enthalpy 8 which moves the liquid in the tank can be brought into contact with the fluid 6 for a long time. Therefore, the gas can be further dissolved in the liquid with high efficiency. Further, in the air-dissolved water generating device, the air inlet port 14 is formed in the injection η 7 ', which is located at the joint portion i 6 of the water supply line 5 constituting the discharge path, and is rushed. The location of the enlarged part. Therefore, it is delivered from the pump 7: ^ through the water supply line 5, and then through the injector 丄7 most = 2. Here, the cross section of the first end flow path of the ejector 17 is set to the cross-sectional area of the first end flow path of the water supply line 5, and the flow rate of the liquid flowing through the water supply line 5 is compared with the ejector 17 The liquid flow rate is faster. The vortex is generated by the ' of the flow rate' and the portion where the air flow person π! 4 rushes to expand A. This thirsty flow is passed through the return line 2 and the working population χ 4 and will stay in the upper end of the tank 2 and suck in with a strong suction pressure of 1361111. Therefore, with this configuration, the amount of the transmitter 17 flowing to the gas worker 8 is increased. Furthermore, the difference in flow rate produces a shearing force in the sprayer 17. This shearing force is applied to the air sucked in through the air inlet 14 by the airflow, whereby the shearing force splits the air bubbles in the liquid delivered to the injector 17 into fine bubbles. The liquid having the fine bubbles is sent to the tank 2. That is, the contact area between the gas and the liquid in the tank is further increased. Further, since the suction pressure due to the difference in the flow rate is high, there is no clogging of the return line 12 in the like. That is, it is not necessary to particularly reduce the inner diameter of the return line 1 2 . Further, the larger the pressure difference ΔP between the pressure P1 in the vicinity of the air flow outlet 13 and the pressure P 0 in the vicinity of the air inlet 14 in the air-dissolved water generating device, the gas remaining in the upper portion of the tank 2 is sucked into the jet. The amount of the device 1 7 is increased. Then, the larger the contact area between the bubble and the ^^, the higher the dissolution efficiency of the gas with respect to the liquid. Therefore, in the present embodiment, the flow path area of the first end of the ejector 17 is set to be larger than the flow path area at the first end of the water supply line 5. ^ It is forced to stay in the upper part of the tank 2 by means of a pump or the like: air circulation. In this case, an air inflow port is formed at the bottom of the trough and then a pump is provided, which is configured to pass the return line 1 • to deliver air to the air inflow port. Further, in the present embodiment, the liquid inflow port 4 is formed at the bottom of the groove. However, as shown in the fourth figure, it is preferable to provide the liquid inflow port 4 on the side wall of the tank 2. The configuration other than the position of the 愔p and the dissolved water generating device in the tank 2 of the ': body flow inlet 4" "the air of the second figure is delivered to the gas of the ejector 17" The contact distance τ is determined to be shorter than the first to second and the second contact distance. The second dissolved water generating device is fixed. Further, this configuration can make the contact suitable for the orientation of the medium, and the second dissolved water generating device 1 has a height of two = two, and the same effect can be obtained even if the air inflow port 14 is disposed at the lower portion of the tube 2. Further, in the present embodiment, the water from the water 7 constituting the discharge path is formed by the Γγ road 5 and the ejector 17 so that the water pressure of the water flowing through the water supply pipe is Takata '1 and is not The discharge path is connected to the water supply pipe by using a pump, and the water of the water supply pipe is used, and the mouth is in the groove 2. In this case, there is no need to activate the pump. (Embodiment 1) FIG. 10 is a perspective view showing an air-dissolving two-component apparatus 1 according to Embodiment 1 of the present invention. Fig. 5 is a schematic view showing an air-dissolved water generating device i according to the embodiment of the present invention. The same applies to the basic configuration of the air-dissolved water generating device 1 of the first and second figures, and the same reference numerals will be given thereto, and the description will be omitted substantially. Too careful & /, 空气 男 男 男 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气 空气
Ill 2、泵7、回流管路12、噴射器17、管路5(圖 未顯不出)、液體流出管路8b、空氣釋放閥1〇 〇、空氣噴射器3 0 0、空氣流入路3 〇工、及固 定裝置2 〇 〇。 槽2係如第六圖所示,由槽下部2 l、及安裝 於槽下部2 L上方的槽上部2㈣構成。 在槽下部2 L之底具備液體流入口 4與液體流 出口 8。在槽下部^之下面設置液體流出管路8 b ’此液體流出管路8b係將自液體流出口 8所流 經,液體導向橫方向。如第十五圖所$,在流 出官路8 b之内部設置往上方延伸之播板8 c。,該 擋板8 C係沿著液體流出管路8 b的長邊方向配 置。如第十六圖所示,擋板8 c之高度被設定為液 體流出管路8b内徑之一半以下。槽下部2匕在上 方具有開π。槽下部2 L具有往上方延伸之撞板2 9如第一圖或第七圖所示,在槽下部2 l橫方向 之外周上端形成有凸緣2 〇乙。 在乜上邛2 U下方具有開口。在槽上部2 口之 :側上面形成在下方延伸而出之隔壁2 6。在槽上 部2 U之上面形成空氣流出口丄3。在槽上部2 口 之上面設置空氣釋放閥1〇◦。在槽上部2U之橫 方向外周下端’形成凸緣2 〇 U。槽上部2 U係配 置於槽下部2 L.之上方。接著凸緣2 〇 L係藉由螺Ill 2, pump 7, return line 12, ejector 17, line 5 (not shown), liquid outflow line 8b, air release valve 1 空气, air ejector 300, air inflow 3 Completion and 2 fixtures. As shown in the sixth drawing, the groove 2 is composed of a groove lower portion 2 l and a groove upper portion 2 (four) attached to the groove lower portion 2 L. At the bottom of the lower portion 2 L of the tank, a liquid inflow port 4 and a liquid outflow port 8 are provided. A liquid outflow line 8b' is disposed below the lower portion of the tank. This liquid outflow line 8b flows from the liquid outflow port 8 and the liquid is directed in the lateral direction. As shown in Fig. 15, a broadcast board 8c extending upward is provided inside the exiting official road 8b. The baffle 8 C is disposed along the longitudinal direction of the liquid outflow line 8 b. As shown in Fig. 16, the height of the baffle 8c is set to be less than one-half of the inner diameter of the liquid outflow pipe 8b. The lower portion 2 of the groove has an opening π above. The lower portion 2 L of the groove has a striker 2 9 extending upward as shown in the first or seventh figure, and a flange 2 is formed at the upper end of the outer portion of the groove lower portion 2 l in the lateral direction. There is an opening below the 邛2 U. In the upper portion of the groove 2, the side wall is formed with a partition wall 26 extending downward from the side. An air outflow port 3 is formed above the upper portion 2 U of the groove. An air release valve 1 is provided above the upper 2 ports of the tank. A flange 2 〇 U is formed at the outer peripheral lower end ' in the lateral direction of the upper portion 2U of the groove. The upper part of the trough 2 U is placed above the lower part of the trough 2 L. Then the flange 2 〇 L is driven by the snail
I3611H 合於凸緣2〇u以固定於槽下部2L。藉此槽2具 有寬長、及向。因此在槽2之内部具有隔壁2 6 與擋板2 9。槽2之内部係藉由隔壁2 6分離成為 混合室2 2與分離室2 3。分離室2 3係藉由擋板 2 9分離成第一副分離室2 3 1與第二副分離室2 3 2° 混合室2 2係被槽2内面與隔壁2 6所劃分之 空間。混合室2 2係為了製成氣體溶解水而設置。 在混合室2 2之底形成液體流入口 4。液體流入口 4安裝有噴射器17。 隔壁2 6係為·了分割混合室2 2與分離室2 3 而設。4言之,隔壁2 6係為了分割混合室2 2與 第一副分離室2 3 1而設。隔壁2 6係沿著槽2的 高度方向而設。又如第六圖所示,隔壁2 6係橫亙 槽2之覓度而設。隔壁2 6之下端係自槽2之底面 拉離而設,藉此以形成連通混合室2 2與第一分離 室231的連通路26P。 第一副分離室2 3 1係為了將經由連通路2 6 P自混合室2 2所輸送之含氣泡氣體溶解水分離為 氣泡與氣體溶解水而設。如第五圖所示,混合室2 2係與第-副分離室2 3丄鄰接而設,藉此混合室 2 2與第-副分離室係沿著槽2的長邊方向配置。 在第-分離室2 3 1之上面設置空氣流出 18 1361111 擋板2 9係為了將分離室2 3分離成第一副分 離室2 3 1與第二副分離室2 3 2而設。如第五圖 或第六圖所示,擋板2 9係沿著槽2之高度方向而 設°又擋板2 9係橫亙槽2之寬度而設。擋板2 9 係配置為具有與隔壁2 6—面2 6 S相向之一面2 9 S。在指板2 9之下端設置導板2 9 L,該導板 2 9 L係自該一面2 9 S朝向隔壁2 6突出,且沿 著槽2之南度方向延伸而出。在擔板2 9之上端中 央形成延伸至上方的延伸板2 9 U。擋板2 9之上 端係自槽2之上面拉離而設,藉此以形成連通第一 分離室2 3 1與第二分離室2 3 2之連通路2 9 P。該擋板2 9係為了將自第一副分離室2 3丄流 入之含氣泡之氣體溶解水分離成氣體與氣體溶^水 而設。· • 第二副分離室2 3 2係為了將自第一副分離室 2 3 1經由連通路2 9 P所輸送之氣體溶解水滯留 而没。在第二副分離室2 3 2之底設置液體流出口 8。液體流出口 8之剖面積係設定為成為第二副分 離室2 3 2之剖面積的1/5以下。 • 第一副分離室2 3 2上端之内壁係以傾斜壁2 6W界定,該傾斜^2 6W係自第—副分離室上端 之内壁呈連續而在下方連續傾斜。在第二副分離室 2 3 2上端設置空氣釋放閥1〇〇。又在第二副分 匕气整流板2 3 2 u,該整流板232 ,自第一副分離室2 3 2之上面往下方 出,且沿著槽2之甚f a ”且鬼I邊方向。該整流板2 3 2 U係 :!?2長邊方向而形成。亦即整流板2 3 2 1]係 w z y及拾板2 9之延伸板2 9 U的寬度 :又又的方向而形成。第—副分離室2 3丄係盥 ❹離室2 3 2鄰接而設,藉此,混合室”’: 槽2 3 1與第二副分離室2 3 2係沿著 j =邊:向而配置。又自第一副分離室231 相^ 室2 3 2係配置於混合室2 2之 之县又’ /σ讀板2 9之高度方向的擋板2 9 J線係和第一副分離室2 3丄與第二 之境界相交。 主 如第二 /泉路--畜丨 此系7係 7之構成 的水經由 7 2係經 2,藉此 係以控制 —端5 1 泵7具備泵入口 7丄與泵出口 7 2。 二圖所示,泵入口71係經由作用為循環 分的配管4 0 〇而與浴槽9 0 〇連接,藉 經由配管4 0 〇與浴槽9 〇 〇相連通。‘ 係將滯留於作用為水供給源之浴槽9 〇 ; 液體流人口 4將液时出至槽2。泵出σ 由水供給管路5與喷射器1 7而連接於样 與槽2之混合室22相連通。該泵; 器C來控制。 噴射器1 7具有與水供給管路5之第 20 1361111 :連,之第-端171和與液體流入口“目連接之 弟:1 72。噴射器1 7與水供給管路5係定義 $出路徑’該噴出路徑用以自泵了輸送液體至槽 :二:在喷射器17之第一端171形成空氣流 入口 1 4 〇 第一,流管路12具有與空氣流出口13相連接之 二::和與空氣流入口14相連接之第二端。藉此 :::路12係和第-副分離室231及第二副分 至2 3 2之上端與噴射器丄7相連通。 β空氣釋放閥1Q0係所謂料標閥。第十四圖 =氣釋放闕100。空氣釋放閥1〇〇係由汽 』0 1與净標1 ◦ 2所構成。在汽缸筒i 0、 内部具有空間。在汽紅筒101形成開口103用 以在汽缸筒1〇1側面之下端連通汽缸 i =空間與第-副分離室231及第二副分離室2 3 2之上部。一方面在汽缸筒2上面形成空氣除去 孔10 4。浮標i 〇 2係配置於汽缸筒丄〇 ^ 部。汽紅筒1 〇 1係設置於第二副分離室2 3 2之 上壁,其位置係在汽缸筒i 〇丄之 分離室…上面更下方之位卜藉此汽 1之開口 1 0 3係較該第二副分離室2 3 2上面的 最高部分更位於設定距離下方。空氣釋放閥 〇 係配置為位於整流板2 3 2 U上方之位置。 二氣喷射器3 Ο 0係安裝於泵7之泵入口 7 1。在空氣噴射器3 〇 〇之一端設置空氣供給口 0 2° 山么t氣流入路3 〇 1具有第一端與第二端,第一. 端係安裝於空氣喷射器3 0 〇之空氣供給口 3 〇 . 2 ’、第二端係位於較槽2之上壁更上方的位置,設 . 置成可吸引空氣供給口 3 0 1之第二端的周圍空 氣。 —固定裝置2 0 0係用以固定槽2或泵7之物。Φ 固定裝置2 Q 〇在上方具有開σ,在開口之緣形成 凸緣201。接著,在固定裝置2〇〇之上配置槽 2以在凸緣2 0 1之上配置槽下部2 L的凸緣2 〇 L。接著’系7被安裝於固定裝置2〇〇,以使泵 7位於槽2下方之位置。 此種空氣溶解水生成裝置1係以如下方式動 作。在泵7起動時,泵7係自吸進口 4 0 3經由作 _ 用為循環流路之一部分的配管4 〇 〇及空氣喷射器 3 0 〇吸進浴槽9 〇 〇之水。流經空氣喷射器3 〇 〇之水在空氣噴射器3 〇 〇内產生壓力。此壓力係 自空氣流入路3 0 1將空氣引進空氣喷射器3 〇 〇 内之力。因此在空氣流入路^卩丄第一端與第二端 · 之間產生壓力差。藉由該壓力差,空氣經由空氣流 入路3 0 1被吸進空氣喷射器3 〇 〇内。被吸進空 22 1361111 氣噴射器3 Ο 0之空氣混合診流經空氣喷射器3 Ο 0之水。藉此,流經空氣喷射器3 0 0之水含有氣 泡。接著泵7係自泵出口 7 2送出泵7内之水。自 泵7所送出之水,經由水供給管路5及噴射器7, 噴出至槽2之混合室2 2中。藉由泵7將水喷出至 混合室2 2内,在混合室2 2内所噴出之水,衝擊 混合室2之壁或隔壁2 6等而彈濺。藉此喷出至混 合室2 2内之水與混合室2内空氣混合。又,泵7 因係在混合室2 2内持續喷出水,故在混合室2 2 μ · .· 内有水滯留。在混合室2内滯留之水經由連通路2 ν,山 Λ 6 Ρ亦流經第一副分離室2 3 1。藉此在第一 ΪΓ分 離室2 3 1亦有水滯留。泵7因係將水持續喷出於 混合室2,故滯留於槽2内之水衝擊槽2之壁等與 業已飛濺之水再次衝擊。再者,因泵7係將水持續 喷出於槽2中,故槽2中之水被自泵7所輸送之水 所攪拌。 藉由此種衝擊,滯留於混合室2 2中之氣體與 水1 1混合。藉由空氣混合於水,可製成在水中含 有大型氣泡的氣體混合水。接著,藉由在混合室2 2之中攪拌水,而於混合室中之水產生剪斷力。剪 -斷力係加諸於混合於水中之大型氣泡。剪斷力係將 大型氣泡分裂成微細氣泡。藉由將大型氣泡分裂成 微細氣泡,氣體變成易於溶解於水·。結·果空氣溶解 於水,藉此可製成氣體溶解水。再者藉由在混合室 23 1361111 2 2之_攪拌水,溶解於水之空氣濃度分布大致成 為均一。結果,混合室2 2中的空氣更加易於溶解 於水。接著,含有氣泡之氣體溶解水係經由連通路 2 6 P被輸送至第一副分離室23 1。 自混合室2 2流至第一副分離室2 3 1之含氣 /包的氣體溶解水進一步溶解微細氣泡。接著,氣體 溶解水係藉由擋板2 9及導板2 9 L朝向上方進行 机動。再者,導板2 9 L係阻礙氣體溶解水在第一 田J刀離至2 3 1中形成渦流。接著,當氣體溶解水 在第一副分離室2 3丄滯留時,第一副分離室2 3 1之水位達到擋板2 9之上端。在水位達到擋板2 9之上端時,氣體溶解水超過擋板2 g之上端,經 由連通路2 9 P流至第二副分離室2 3 2。詳言 之,在水位達到擋板2 9上端時,氣體溶解水被擋 板2 9的延伸板2 9 U所分又,經由連通路2 9 p 流至第二副分離室2 3 2。 此時流經連通路2 9 P之氣體溶解水曝露於第 一副分離室2 3 1及第二副分離室2 3 2上部之空 間。藉此大多含氣泡之氣體溶解水,藉由曝露於^ 一田彳分離室2 3 1及第二副分離室2 3 2上部之空 間而使氣泡分離,並分成已溶解氣體之液體、與空 氣。接著被分離之氣泡與滯留於第一副分離室2 2 1上部的氣體統合,而在第—副分離室2 3 i及第 24 二副分離室2 3 2上部有空氣滯留。又由於氣體溶 解水被擋板2 9之延伸板2 9 U所分叉,自第—副 分離室2 3 1流至第二副分離室2 3 2,故可防止 在第二副分離室2 3 2之上部產生與氣體溶解水之 渦流。藉此流至第二副分離室2 3 2之含有氣泡的 氣體溶解水不被渦流所妨礙,而分離成氣體與氣體 溶解水。又因藉由導板29L、延伸板29u而= 礙渦流之形成,故可防止因渦流所產生大型氣泡之 流出。 流至第二副分離室2 3 2之氣體溶解水在藉由 整流板2 3 2 U使流動在經整流之狀態下,將流動 方向朝向下方。如此一來,流至第二副分離室2 3 2之氣體溶解水經由液體流出口 8流至液體流出管 ,8 b。在此,液體流出口 8之剖面積因係設定為 第二副分離室2 3 2之剖面積的1/5以下,故流 二副分離室2 3 2之氣體溶解水具有較流至: -’ l出口 8之氧體溶解水流速更慢的流速。該緩慢 的流速不會妨礙氣體溶解水所含氣泡的浮上。又Γ 流至液體流出管路8 b之氣體溶解水係如第十六圖 所不,藉由擋板8 c,而被賦予沿著液體流出管路 8乜之長邊方向的流動方向。又,擋板8 係阻礙 ,液體流出管路8 b中氣體溶解水發生渦流。因 此即使在氣體溶解水中存在微細氣泡時,微細氣 泡被統合難以產生大型泡,而可抑制在自槽取出之 25 ,粗冷解水中混人A型氣泡。流經液體流出管路8 :氣體溶解水,經由作用為循環流路之一部分的 配官4 0 1自液體排放口 4 〇 2輸送至浴槽9 〇 0被輸^:至A槽9 0 Q的氣體溶解水曝露於大氣 昼m溶解於氣體溶解水巾之水的空氣產生微 細乳泡。該微細氣泡由於微細故停留於水中。如此 一來含有微細氣泡之熱水係供應至浴槽等。一方 面’在槽2中不溶解於水之空氣係以氣泡浮出槽2 上方而分離,該氣泡與滞留於槽上部的氣體—起滯 一方面,滯留於第一副分離室2 3 1及第二副 分離室2 3 2上部之空氣經由回流管路丄2被輸: 至喷射器1 7。詳言之,在空氣溶解水生成裝置1 之運作中,泵7係經由水供給管路5、噴射器1 7、 及液體流入口 8持續供給水於槽2。通過噴射器工 7自泵7輸送至混合室2 2之水,對空氨产Λ 4產生壓力。在該空氣流入口 14與空 3間之壓力差將滯留於槽2上部之空氣吸進回流管 路1 2。被吸進回流管路丄2之空氣,經由空=二 入口 1 4被輸送至喷射器1 7内。 %敬 如此一來,滯留於第一副分離室2 3丄與—_ 副分離室2 3 2之上部的空氣,輸送至被定義:: 回流管路1 2及喷出路徑的喷射器i 7。 ‘“、 彌送至噴 26 射。。1 7之空氣成為氣泡,與自泵 再度噴出至混合室2 2中。 、出之水一起 方面,因水自栗7持續噴出至混合室” “體溶解水在流至液體流出口 8之 , 空氣釋放間100。流至空氣釋放心〇 = :=2上推至上方。藉此浮標102係:= 汽缸筒101内部之間開放位r 副置的情況下,若在第- 步有…, 副分離室2 3 2之上部進一 工切騎,第—副分離室2 _ ξ ^ 9 Q 〇 , 丄/、乐一田1J 分 一 2 3 2之水位降低。接著,第一副分 閱室2 3 2之水位在位於較蝴放 經由開口 103…f 時’槽内空氣 ^氣釋放閥1。〇的空氣經由空= :::r。藉―部將適當 回流發!Γ氣溶解水生成裂置1具備- 2=::離室2 3 2上部之空氣輸送至定義作 離室2:=Γ器17。因此’滞留於第-副分 栗7輪:分離室23·2上部的空氣與自 此5至2 2之水混合。接著,混合著空 27 1361111 =之水噴出至混合室2 2。亦即 離室23工及第二副分 第, 於混合室” n ^ 3 2上部的空氣再次 效率溶解二!水。藉此可獲得構成為以高 旱-解空亂於水的空氣溶解水生成裝置i。 混合室22下端部形成空氣流入 :在此情形該回流管路12之一端連接該空 σ 1 4。藉此,可將滯留於第-副分離室2 3 1及第二副分離室2 3 2上 至2 室22中溶解於水。上部的空氣再度在現合 又^明之空氣容解水生成裝η具有 23。在該分離室23自含痛μ 矛4之乳泡’並分成溶解氣體之液體 此變成難以使大徑的氣泡自液體流出 此將該空氣溶解水生成裝置χ連接“出。: 滞留於浴槽9 0 〇之水藉由栗7卜 〇,將 ^ Λ' ^ m 1 - 口於空氣溶解水 广置丄,藉由將自液體流出口 解水回至浴槽9 go進行循環 工乳岭 01 ^ ^ ^ m v + Μ更在構成附有空 風Ά水生成裝置#槽時’亦難 熱水中混入大徑之氣泡,可防止=〜泡的 低。 」防止冷槽中的水品質降 又本發明空Α溶解水生成裝置i 室232之上壁“下方呈傾斜之傾斜離 疋義。接者’空*落解水生成聚置1具有空氣釋: 28 丄則111 閱]Π π 5玄空氣釋放閥1 〇 〇係設置於傾斜壁2 6 W ° 含 β 乂 亦即’空氣釋放閥1 〇 〇之開口 1 〇 3係位 於車χ第一副分離室2 3 1之上壁更下方之位置。因 ’在第一副分離室2 3 1與第二副分離室2 3 2 =上。卩汴留較設定量更多之空氣時,空氣經由空氣 放閥1 0 Q被釋放。藉此可將設定量之空氣經常 一 3於弟一副分離室2 3丄。因此,可將滯留於第 -釗刀離室2 3 1之上部的空氣經由回流管路工2 經常輪送至噴射器1 7。 -®再者,空氣釋放閥1 0 0具備汽缸筒1 與 :祆10 2。在汽缸筒1 0 1之側面下端形成開口 ”3。因此該開口 103係開口於汽缸筒⑴ 方向。因此,在氣泡自流至第二副分離室2 3 =方的氣體溶解水浮出至上方時,氣泡被汽缸 闻1 ◦ 1下面阻礙往上方 乃之移動。位於汽缸筒1 〇 1下面位置之氣泡係沿著汽 百α缸同之下面1 0 1 B移 動,且移動至第一副分離室 _ 主丄及弗一副分離室 2 3 2之上方。如此一來,力 — 在弟一副分離室232 中之氣泡,首先係在第一副 、a — 〇 J刀離至2 3 1及第二副 分離室232之上方移動。i 1 '、後’在弟一副分離室 231及第二副分離室^ ^ ^ D± 产 d 2之上部滯留設定量之 空氣時,空氣經由在橫方向 J栗已開口之開口 1 自空氣釋放閥100釋出样 將設定量的空氣滯留於笫一 _·、 u此、'二吊了 乐一副分離室2 3 1之上 1361111 部。因此可將無法溶解於水的 以溶解。 空氣再次在混合室 予 又 —副分 第二副 之上方 分離室 集於空 1具備 端設置 9 S朝 向延伸 氣泡的 3 1中 之向度 —副分 氣溶解 二乳釋放閥1 〇 0係配置於定義第 離室2 3 2之上面的傾斜壁2 6 w。因此在 分離室2 3 2内移動至第二副分離室2 3 2 的氣泡係沿著傾斜壁2 6 w,移動至第一副 ^ 3 1之上部。因此可獲得構成為使空氣收 氣流出口 1 3的空氣溶解水生成裝置丄。 又,本實施形態之空氣溶解水生成裝置 一隔壁26與-擋板29。在擋板29之下 一導板2 9 L,該導板2 9 L係自該一面2 向隔壁2 6延伸而出,且沿著槽2之高度方 而出。因此,流經第一副分離室2 3丄之含 氣體溶解水,在渦流難以在第一副分離室2 產生之狀態下,係沿著第一副分離室2 3 1 方向流動。因此,大徑之氣泡難以流出至第 離室2 3 2側,在自液體流出口 8流出之空 水,大從之氣泡混入亦變少。 又,本實施形態之空氣溶解水生成裝置丄係具 備空氣喷射器30〇與空氣流入路301。接著, 本實施形態之空氣溶解水生成裝置1係構成為,經 由空氣流入路3 0 1輸送經吸進之空氣於流至&氣 噴射器3 0 0之水。因此可預先混合空氣於自喷出 30 1361111 路徑輸送至混合室2 2之水。藉此可獲得構成為以 高效率製成氣體溶解水的空氣溶解水生成裝置1。 在此,自空氣釋放閥所釋放空氣之每單位時間 之體積宜設定為自該喷出路徑所噴出之水所含該空 氣每單位時間體積之2 0 %以上。再者,自空氣釋 放閥所釋放空氣之每單位時間之體積更宜為設定為 自該喷出路徑所喷出之水所含該空氣每單位時間體 積之8 0 %以下。 在此,氣體之溶解速度係如上述,以氣液之接 觸面積與氣體之濃度梯度之乘積,以次式表示I3611H is fitted to the flange 2〇u to be fixed to the lower portion 2L of the groove. Thereby, the groove 2 has a width and a length. Therefore, there is a partition wall 26 and a baffle 2 9 inside the tank 2. The inside of the tank 2 is separated into a mixing chamber 2 2 and a separation chamber 23 by a partition wall 26 . The separation chamber 23 is separated into a first sub-separation chamber 2 3 1 and a second sub-separation chamber 2 3 by a baffle 209. The mixing chamber 2 2 is partitioned by the inner surface of the tank 2 and the partition wall 26. The mixing chamber 22 is provided to form a gas-dissolved water. A liquid inflow port 4 is formed at the bottom of the mixing chamber 22. The liquid inlet 4 is provided with an injector 17. The partition wall 26 is provided to divide the mixing chamber 2 2 and the separation chamber 2 3 . In other words, the partition wall 26 is provided to divide the mixing chamber 2 2 and the first sub-separation chamber 23 1 . The partition wall 6 6 is provided along the height direction of the groove 2. Further, as shown in the sixth drawing, the partition wall 26 is provided with the width of the horizontal groove 2. The lower end of the partition wall 26 is pulled away from the bottom surface of the tank 2, thereby forming a communication passage 26P that communicates the mixing chamber 2 2 with the first separation chamber 231. The first sub-separation chamber 213 is provided to separate the bubble-containing gas-dissolved water transported from the mixing chamber 22 through the communication passage 26p into bubbles and gas-dissolved water. As shown in Fig. 5, the mixing chamber 22 is disposed adjacent to the first-stage separation chamber 213, whereby the mixing chamber 22 and the first-stage separation chamber are disposed along the longitudinal direction of the groove 2. An air outflow is provided on the upper surface of the first separation chamber 213. The ventilator 209 is provided to separate the separation chamber 2 3 into the first sub-separation chamber 213 and the second sub-separation chamber 233. As shown in Fig. 5 or Fig. 6, the baffle plate 9 is provided along the height direction of the groove 2 and the baffle plate 9 is the width of the traverse groove 2. The baffle 2 9 is configured to have a surface facing one side of the partition wall 6 6 2 6 S 2 9 S. A guide plate 9 9 L is provided at a lower end of the fingerboard 2 9 , and the guide plate 9 9 L protrudes from the one side 2 9 S toward the partition wall 26 and extends in the south direction of the groove 2. An extension plate 2 9 U extending to the upper side is formed at the center of the upper end of the support plate 29. The upper end of the baffle plate 29 is pulled away from the upper surface of the groove 2, thereby forming a communication path 2 9 P that communicates the first separation chamber 213 and the second separation chamber 233. The baffle plate 29 is provided to separate the bubble-containing gas-dissolved water flowing from the first sub-separation chamber 23 into a gas and a gas-soluble water. • The second sub-separation chamber 2 3 2 is not used to trap the dissolved water from the first sub-separation chamber 2 3 1 via the communication passage 2 9 P. A liquid outflow port 8 is provided at the bottom of the second sub-separation chamber 233. The cross-sectional area of the liquid outflow port 8 is set to be 1/5 or less of the sectional area of the second sub-separation chamber 2 3 2 . • The inner wall of the upper end of the first sub-separation chamber 2 3 2 is defined by an inclined wall 26W which is continuous from the inner wall of the upper end of the first-second separation chamber and continuously inclined downward. An air release valve 1 is provided at the upper end of the second sub-separation chamber 233. Further, in the second sub-half gas rectifying plate 2 3 2 u, the rectifying plate 232 is discharged downward from the upper surface of the first sub-separating chamber 2 3 2 and along the groove 2 in the direction of the ghost I side. The rectifying plate 2 3 2 U is formed in the longitudinal direction of the bearing 2, that is, the rectifying plate 2 3 2 1] is the width of the extension plate 2 9 U of the wzy and the pickup plate 9 9 : it is formed in another direction. The first-second separation chamber 2 3 is disposed adjacent to the chamber 2 3 2 , whereby the mixing chamber “′: the tank 2 3 1 and the second sub-separation chamber 2 3 2 are along the j=edge: Configuration. Further, from the first sub-separation chamber 231, the chamber 2 2 2 is disposed in the county of the mixing chamber 22, and the baffle 2 9 J line and the first sub-separation chamber 2 in the height direction of the / σ reading plate 209 3丄 intersects with the second realm. Mainly as the second / spring road - the animal is the 7-series 7 of the water through the 7 2 system 2, whereby the control - end 5 1 pump 7 has a pump inlet 7 丄 and pump outlet 7 2 . As shown in the second figure, the pump inlet 71 is connected to the bath 90 by means of a pipe 40 作用 which acts as a circulation, and communicates with the bath 9 〇 via the pipe 40 〇. ‘The system will stay in the bath 9 that acts as a water supply source; the liquid stream population 4 will flow out to the tank 2. The pumping σ is connected to the mixing chamber 22 of the tank 2 by the water supply line 5 and the ejector 17 . The pump; the device C to control. The ejector 17 has a second end 171 connected to the water supply line 5, and a first end 171 and a liquid connection to the liquid inlet: 1 72. The ejector 17 and the water supply line 5 define $ The exit path 'the discharge path is for self-pumping to transport the liquid to the tank: two: at the first end 171 of the injector 17 forms an air flow inlet 1 4 〇 first, the flow line 12 has a connection with the air flow outlet 13 Two:: and a second end connected to the air inflow port 14. Thereby: the path 12 and the first-second separation chamber 231 and the second sub-portion to the upper end of the 2 3 2 are in communication with the injector 丄7. The β air release valve 1Q0 is a so-called material standard valve. Figure 14 = air release 阙 100. The air release valve 1 is composed of a steam 0 0 1 and a net standard 1 ◦ 2. In the cylinder tube i 0, the inside has In the steam red cylinder 101, an opening 103 is formed for communicating the cylinder i=space with the upper portion of the first-second separation chamber 231 and the second sub-separation chamber 2 3 at the lower end of the side of the cylinder barrel 1〇1. 2, an air removing hole 104 is formed on the upper surface. The buoy i 〇 2 is disposed in the cylinder bore portion. The steam red cylinder 1 〇 1 is disposed in the second sub-separating chamber 2 3 2 The upper wall is located at the lower part of the separation chamber of the cylinder bore i... the opening 1 0 3 of the steam 1 is located at a set distance more than the highest part of the second secondary separation chamber 2 3 2 Below, the air release valve is configured to be located above the rectifying plate 2 3 2 U. The two gas injector 3 Ο 0 is mounted to the pump inlet 7 1 of the pump 7. An air supply is provided at one end of the air injector 3 Port 0 2° Mountain tt air inlet 3 〇1 has a first end and a second end, the first end is installed in the air ejector 3 0 〇 air supply port 3 〇. 2 ', the second end is located The position above the upper wall of the tank 2 is set to attract the surrounding air of the second end of the air supply port 310. The fixing device 200 is used to fix the groove 2 or the pump 7. Φ Fix The device 2 Q has an opening σ at the upper side, and a flange 201 is formed at the edge of the opening. Next, the groove 2 is disposed above the fixing device 2〇〇 to arrange the flange 2 of the groove lower portion 2 L above the flange 210 〇L. Then the 'system 7 is mounted on the fixture 2〇〇 so that the pump 7 is located below the tank 2. This air dissolves The generating device 1 operates as follows: When the pump 7 is started, the pump 7 is sucked into the bath 9 from the suction inlet 4 0 3 via the pipe 4 〇〇 which is used as a part of the circulation flow path and the air ejector 3 0 The water flowing through the air ejector 3 generates pressure in the air ejector 3 。. This pressure is the force that is introduced into the air ejector 3 from the air inflow path 301. A pressure difference is generated between the first end and the second end of the air inflow path. By this pressure difference, air is sucked into the air injector 3 〇 through the air inflow path 301. Being sucked into the air 22 1361111 Air ejector 3 Ο 0 The air mix is passed through the air ejector 3 Ο 0 water. Thereby, the water flowing through the air ejector 300 contains air bubbles. Pump 7 then delivers water from pump 7 from pump outlet 7 2 . The water sent from the pump 7 is discharged into the mixing chamber 22 of the tank 2 via the water supply line 5 and the ejector 7. The water is ejected into the mixing chamber 22 by the pump 7, and the water ejected in the mixing chamber 2 2 is splashed by impinging on the wall of the mixing chamber 2 or the partition wall 26 or the like. The water sprayed into the mixing chamber 22 is thereby mixed with the air in the mixing chamber 2. Further, since the pump 7 continuously discharges water in the mixing chamber 22, water is retained in the mixing chamber 2 2 μ···. The water remaining in the mixing chamber 2 passes through the communication passage 2 ν, and the mountain Λ 6 Ρ also flows through the first sub-separation chamber 23 1 . Thereby, water is also retained in the first separation chamber 2 3 1 . Since the pump 7 continuously sprays water out of the mixing chamber 2, the water retained in the tank 2 impinges on the wall of the tank 2 and the like, and the splashed water is again hit. Further, since the pump 7 continuously sprays water into the tank 2, the water in the tank 2 is stirred by the water supplied from the pump 7. By this impact, the gas retained in the mixing chamber 22 is mixed with the water 1 1 . By mixing air with water, it is possible to produce a gas mixed water containing large bubbles in water. Next, the water in the mixing chamber is sheared by agitating the water in the mixing chamber 22. Shear-breaking force is applied to large bubbles mixed in water. The shearing force splits large bubbles into fine bubbles. By splitting the large bubble into fine bubbles, the gas becomes easily dissolved in the water. The knot and fruit air are dissolved in water, whereby the gas is dissolved in water. Further, by stirring the water in the mixing chamber 23 1361111 2 2, the air concentration distribution dissolved in water is substantially uniform. As a result, the air in the mixing chamber 22 is more easily dissolved in water. Next, the gas-dissolved water containing the bubbles is sent to the first sub-separation chamber 23 1 via the communication path 2 6 P. The gas-containing/packaged gas dissolved in water from the mixing chamber 2 2 to the first sub-separation chamber 2 3 1 further dissolves the fine bubbles. Next, the gas-dissolved water is maneuvered upward by the baffle plate 29 and the guide plate 29L. Further, the guide plate 2 9 L blocks the gas-dissolved water from forming a vortex in the first field J knife to be 2 3 1 . Next, when the gas-dissolved water is retained in the first sub-separation chamber 23, the water level of the first sub-separation chamber 213 reaches the upper end of the baffle 29. When the water level reaches the upper end of the baffle 2 9 , the gas dissolved water exceeds the upper end of the baffle 2 g and flows through the communication path 2 9 P to the second sub-separation chamber 2 3 2 . More specifically, when the water level reaches the upper end of the baffle plate 29, the gas-dissolved water is divided by the extension plate 2 9 U of the baffle plate 29, and flows to the second sub-separation chamber 2 3 2 via the communication path 2 9 p. At this time, the gas dissolved water flowing through the communication path 2 9 P is exposed to the space in the upper portion of the first sub-separation chamber 2 3 1 and the second sub-separation chamber 2 3 2 . Thereby, the gas containing a large amount of bubbles dissolves the water, and the bubbles are separated by being exposed to the space in the upper portion of the separation chamber 2 31 and the second separation chamber 2 3 2, and are separated into a liquid in which the gas is dissolved, and the air. . Then, the separated bubbles are integrated with the gas remaining in the upper portion of the first sub-separation chamber 2 2 1 , and air is retained in the upper portion of the first sub-separation chamber 2 3 i and the 24th sub-separation chamber 2 3 2 . Further, since the gas dissolved water is branched by the extension plate 2 9 U of the baffle plate 29, the second sub-separation chamber 2 is prevented from flowing from the first-second separation chamber 213 to the second sub-separation chamber 2 3 2 . The upper part of 3 2 produces a vortex with the dissolved water of the gas. Thereby, the gas-dissolved water containing bubbles which flows into the second sub-separation chamber 2 3 2 is not disturbed by the eddy current, and is separated into gas and gas-dissolved water. Further, since the guide plate 29L and the extension plate 29u prevent the formation of eddy currents, it is possible to prevent the outflow of large bubbles due to the eddy current. The gas-dissolved water flowing to the second sub-separation chamber 2 3 2 flows in a rectified state by the rectifying plate 2 3 2 U, and the flow direction is directed downward. As a result, the gas dissolved water flowing to the second sub-separation chamber 2 3 2 flows to the liquid outflow pipe 8 b via the liquid outflow port 8. Here, since the cross-sectional area of the liquid outflow port 8 is set to be less than 1/5 of the sectional area of the second sub-separation chamber 2 3 2, the gas dissolved water of the second sub-separation chamber 2 3 2 has a relatively large flow to: - ' l The oxygen flow rate of the outlet 8 is slower. This slow flow rate does not prevent the floating of the bubbles contained in the dissolved water of the gas. Further, the gas-dissolved water flowing to the liquid outflow line 8b is as shown in Fig. 16, and is provided with a flow direction along the longitudinal direction of the liquid outflow line 8乜 by the baffle plate 8c. Further, the baffle 8 is blocked, and the gas-dissolved water in the liquid outflow line 8b is vortexed. Therefore, even when fine bubbles are present in the gas-dissolved water, it is difficult to generate large bubbles by the integration of the fine bubbles, and it is possible to suppress the mixing of the A-type bubbles in the crude cold-dissolved water. Flowing through the liquid outflow line 8: the gas dissolves the water, and is transported from the liquid discharge port 4 〇2 to the bath through the liquid discharge port 4 〇2 which acts as a part of the circulation flow path. 〇0 is transferred: to the A tank 9 0 Q The gas dissolved in water is exposed to the atmosphere, and the air dissolved in the water of the gas-dissolving water towel produces fine emulsions. The fine bubbles stay in the water due to the fineness. In this way, the hot water containing fine bubbles is supplied to the bath or the like. On the one hand, the air which is not dissolved in the water in the tank 2 is separated by the bubble floating tank 2, and the gas bubbles lag with the gas remaining in the upper portion of the tank, and is retained in the first sub-separation chamber 2 3 1 and The air in the upper portion of the second sub-separation chamber 2 3 2 is sent via the return line 丄 2 to the ejector 17 . In detail, in the operation of the air-dissolved water generating apparatus 1, the pump 7 continuously supplies water to the tank 2 via the water supply line 5, the ejector 17 and the liquid inflow port 8. The water sent from the pump 7 to the mixing chamber 22 by the ejector 7 generates pressure on the empty ammonia Λ4. The pressure difference between the air inflow port 14 and the air 3 draws the air remaining in the upper portion of the tank 2 into the return pipe 12 . The air sucked into the return line 丄2 is sent to the ejector 17 via the air = two inlets 14. In this way, the air remaining in the first sub-separation chamber 2 3 丄 and the _ sub-separation chamber 2 3 2 is transported to the ejector i 7 defined as: the return line 12 and the discharge path. . '", the air is sent to the spray 26. The air of the air becomes a bubble, and is again ejected from the pump to the mixing chamber 22. In terms of the water, the water continues to be ejected from the pump 7 to the mixing chamber. The dissolved water flows to the liquid outflow port 8, and the air releases the chamber 100. The flow to the air release heart 〇 = :=2 is pushed up to the top. The buoy 102 is: = the open position r between the cylinder barrel 101 is disposed. In the case, if there is ... in the first step, the upper part of the sub-separation chamber 2 3 2 enters a work-cutting, the first-stage separation chamber 2 _ ξ ^ 9 Q 〇, 丄/, Le Yitian 1J points one 2 3 2 The water level is lowered. Then, the water level of the first sub-dividing room 2 3 2 is located in the air in the tank through the opening 103...f. The air in the tank is via the air = ::: r. The part will be properly recirculated! The helium dissolved water is generated by the split 1 with - 2 =:: the air from the upper part of the chamber 2 3 2 is transported to define the chamber 2: = the sputum 17. Therefore, 'stayed in the first - side split 7 rounds: the air in the upper part of the separation chamber 23·2 is mixed with the water from 5 to 2 2. Then, the water is mixed with the water 27 1361111 = water is sprayed out to the mixing chamber 2 2 , that is, the chamber 23 and the second pair The first, in the mixing chamber "n ^ 3 2 upper air again dissolved efficiency of two! Water. Thereby, it is possible to obtain an air-dissolved water generating device i configured to be highly dry-deficient in water. The lower end portion of the mixing chamber 22 forms an inflow of air: in this case, one end of the return line 12 is connected to the space σ 14 . Thereby, the water retained in the first-second separation chamber 213 and the second sub-separation chamber 233 to the second chamber 22 can be dissolved in water. The air in the upper part is again in the air and the water is formed in the water. In the separation chamber 23, the emulsion containing the pain μ spear 4 and divided into a liquid of a dissolved gas becomes difficult to cause a large-diameter bubble to flow out from the liquid. This connects the air-dissolved water generating device to "out.": stays in the bath 9 0 〇 水 藉 藉 栗 栗 栗 栗 栗 栗 栗 栗 ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ mv + Μ 在 构成 构成 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附 附The upper wall of the open water dissolving water generating device i chamber 232 is inclined downward from the bottom. The picker 'empty* falls into the water to generate the aggregate 1 has air release: 28 丄 then 111 read] Π π 5 mysterious air release The valve 1 is disposed on the inclined wall 2 6 W ° The opening 1 〇 3 of the air release valve 1 is located at a position lower than the upper wall of the first separation chamber 2 3 1 of the rut. Because 'in the first sub-separation chamber 213 and the second sub-separation chamber 2 3 2 =. When the air is trapped more than the set amount, the air The air release valve 1 0 Q is released. Thereby, the set amount of air can be frequently smashed into a pair of separation chambers 2 3 丄. Therefore, the air remaining in the upper portion of the first boring tool away from the chamber 2 3 1 can be retained. It is frequently routed to the injector 1 via the return line 2. -® Further, the air release valve 100 has a cylinder bore 1 and a bore 10 2 . An opening "3 is formed at the lower end of the side of the cylinder bore 1 0 1". Therefore, the opening 103 is opened in the cylinder bore (1) direction. Therefore, when the bubble is self-flowing to the second sub-separation chamber 2 3 = the gas dissolved water floats upward, the bubble is blocked by the cylinder 1 ◦ 1 and the upper side is moved upward. The bubble located at the lower position of the cylinder barrel 1 〇 1 moves along the lower side of the cylinder α cylinder and the lower side 10 1 B, and moves to the upper side of the first sub-separation chamber _ main 丄 and the detachment chamber 2 3 2 . In this way, the force - the bubble in the separation chamber 232 of the younger brother is first moved above the first pair, the a - 〇 J knife is moved to the 2 3 1 and the second sub-separation chamber 232. When i 1 ', after 'the second pair of separation chambers 231 and the second sub-separation chamber ^ ^ ^ D ± the upper part of the production d 2 retains a set amount of air, the air passes through the opening 1 in the transverse direction J from the air The release valve 100 releases a sample to hold a set amount of air in the first and second portions of the first and second separation chambers 2 3 1 . Therefore, it is not possible to dissolve in water to dissolve. The air is again in the mixing chamber, and the separation chamber is placed above the second pair. The separation chamber is set in the air 1 and the end is set to 9 S toward the extended bubble. The dip-side dissociation dissolving the second milk release valve 1 〇 0 configuration The inclined wall 2 6 w above the first chamber 2 3 2 is defined. Therefore, the bubble moving to the second sub-separation chamber 2 3 2 in the separation chamber 213 moves along the inclined wall 260w to the upper portion of the first sub-III. Therefore, an air-dissolved water generating device 构成 configured to allow the air to be discharged from the air outlet 13 can be obtained. Further, the air-dissolved water generating device of the present embodiment has a partition wall 26 and a baffle plate 29. Below the baffle 29, a guide plate 29 L is extended from the one side 2 to the partition wall 26 and along the height of the groove 2. Therefore, the gas-containing dissolved water flowing through the first sub-separation chamber 2 3 流动 flows in the direction of the first sub-separation chamber 2 3 1 in a state where the eddy current is hard to be generated in the first sub-separation chamber 2 . Therefore, it is difficult for the large-diameter air bubbles to flow out to the side of the first chamber 2 3 2 , and the air which flows out from the liquid outflow port 8 is less likely to be mixed with the air bubbles. Further, the air-dissolved water generating device of the present embodiment is provided with an air ejector 30A and an air inflow path 301. Next, the air-dissolved water generating apparatus 1 of the present embodiment is configured to transport the sucked air through the air inflow path 301 to the water flowing into the & gas ejector 300. Therefore, the air can be pre-mixed to the water supplied to the mixing chamber 22 from the path of the spray 30 1361111. Thereby, the air-dissolved water generating apparatus 1 configured to produce the gas-dissolved water with high efficiency can be obtained. Here, the volume per unit time of the air released from the air release valve is preferably set to be more than 20% of the volume per unit time of the air contained in the water ejected from the discharge path. Further, the volume per unit time of the air released from the air release valve is preferably set to be less than 80% of the volume per unit time of the air discharged from the discharge path. Here, the gas dissolution rate is as described above, and is expressed as a product of the gas-liquid contact area and the gas concentration gradient.
Cv=KL · a · ( C * - C ) C v :溶解速度 K L :總括物質移動係數 ' a :接觸面積 C * :飽和溶解氣體濃度 C:溶解氣體濃度 亦即,氣體之溶解速度C v係仰賴於接觸面積 α與飽和溶解氣體濃度C +。 然而,波義耳定律係: 壓力X體積=一定 1361111 因此壓力變大時,氣體體積變小。一方面,在 質量作用之定律(化學平衡定律)中,(氣體濃度) + (溶於液體之氣體濃度)為一定。因此氣體濃度變 高時,溶解於液體之氣體濃度亦變高。亦即如周知 之亨利定律(henry’ s 1 aw),可藉由提 高氣體分壓來提高液體中氣體之飽和溶氧濃度。換 言之,可藉由提高氣體之濃度與壓力來提高液體中 氣體之飽和溶氧濃度。 因此吾人首先發現混合空氣於自液體流入口流 入之液體時,藉由積極地進行溶解槽2之排氣促進 氣體之更換,可使大多空氣溶解於槽2中之水。 考量空氣溶解水生成裝置1對浴槽的適用,而 使空氣中之氧溶解於水,就水中溶氧濃度予以調 查。表一顯示輸送至槽2中之空氣量,與自空氣釋 放閥1 0 0所排氣之空氣量間的比率。亦即顯示由 調整空氣釋放閥之排氣量所致水中溶氧濃度的比 率。此外,輸送至槽2中的空氣量及自空氣釋放閥 1 0 0所排氣的空氣量,係藉由變換自空氣釋放閥 1 0 0所排出空氣之量、與輸送至空氣喷射器3 0 0之氣體量之比來改變。 32 【表- 空氣排β.比 如第十七圖及第十八圖所示 ,積極地排氣15分鐘以 ;1敌閥 二20心上時,*中溶氧濃度二非氣 亦即溶解槽2内之氧分壓提☆ C飽和:狀秦: 於水。 土棱阿,可確認更多氧溶] 根據此種實驗,在空氣溶Cv=KL · a · ( C * - C ) C v : dissolution rate KL : total material movement coefficient ' a : contact area C * : saturated dissolved gas concentration C: dissolved gas concentration, that is, gas dissolution rate C v Rely on the contact area α and the saturated dissolved gas concentration C + . However, Boyle's law: Pressure X volume = a certain 1361111 Therefore, when the pressure becomes large, the gas volume becomes small. On the one hand, in the law of mass action (chemical equilibrium law), (gas concentration) + (concentration of gas dissolved in liquid) is constant. Therefore, when the gas concentration becomes high, the concentration of the gas dissolved in the liquid also becomes high. That is, as well known as Henry's 1 aw, the saturated dissolved oxygen concentration of the gas in the liquid can be increased by increasing the partial pressure of the gas. In other words, the saturated dissolved oxygen concentration of the gas in the liquid can be increased by increasing the concentration and pressure of the gas. Therefore, when we first find that the mixed air flows into the liquid from the liquid inlet, the gas in the tank 2 can be dissolved in the tank 2 by actively performing the replacement of the exhaust gas in the dissolution tank 2. Considering the application of the air-dissolved water generating device 1 to the bath, the oxygen in the air is dissolved in the water, and the dissolved oxygen concentration in the water is investigated. Table 1 shows the ratio of the amount of air delivered to the tank 2 to the amount of air exhausted from the air release valve 100. That is, the ratio of dissolved oxygen concentration in water caused by adjusting the amount of exhaust of the air release valve is shown. Further, the amount of air delivered into the tank 2 and the amount of air exhausted from the air release valve 100 are converted by the amount of air discharged from the air release valve 100 and sent to the air injector 30. The ratio of the amount of gas of 0 changes. 32 [Table - Air discharge β. For example, as shown in the seventeenth and eighteenth figures, actively exhaust for 15 minutes; 1 when the enemy valve is 20 hearts, * dissolved oxygen concentration is not a gas, that is, dissolution tank 2 within the oxygen partial pressure ☆ C saturation: like Qin: in water. Earth ridge, can confirm more oxygen solubility] According to this experiment, dissolved in air
氧濃度 _XLi_〇 -~ΛΑ,_〇ι ^~λ1^5ι 18. 5 空氣釋放閥1〇〇所排氣之空氣每單位時間i: =定為經由水供給管路5,以混合有空氣之水方 V入於槽2内之空氣每單位量之2〇%以 將氣體排氣量設定於給氣量之2 0%以上,.相幸; 氮對水溶解度更高之氧溶解量變多,液體5中氧 解量變多。因此可生成氧之溶解濃度充分高的液 此外,在設定空氣釋放閥i 〇 〇所致氣體之排 氣量導入溶解槽2内之空氣給氣量2 〇 %以上的具 體手段、方法方面可例舉增大氣體導入噴射器3 〇 33 1361111 所致氣體的擷取量。又在空氣釋放閥^ Q 〇中藉由 調整氣體除去口 3 5之開口形狀及面積亦可得相同 效果。接著,藉由適宜選擇該等特徵亦可得相同效 果。再者藉由組合該等特徵亦可得相同效果。 · (實施形態二) 第十九圖、第二十圖顯示關於本發明實施形態 一之空氣溶解水生成裝置1的立體圖。此外,在與 實施形態一相同構成係賦予相同符號,相同構成2 說明在此省略。本實施形態之空氣溶解水生成裝置· 1具備:槽2、泵7、回流管路1 2、喷射器丄7直 管路5 (圖未顯示出)、液體流出管路8 b、空氣釋 放閥1 0 0、空氣噴射器3 〇 〇及空氣流入:『 I 〇 二義噴射器3 0 0係安裝於泵7之泵入口 1。在空氣喷射器3 ◦ 〇之一端設置空氣供給 ’另-端係在|7周邊之上端部背面側插入於 固定裝置2 〇 〇内側。接著其係構成為,經由 流入路3 0丄輸送已吸進之空氣於流至空氣噴:: 3 0 0之水。因此,可預先混合空氣於 、日口口 室2 2之水。藉此可獲得構成為以高效‘製成二 溶解水的空氣溶解水生成裝置1。 、體 又由於其係構成為經由空氣流^3() 已吸進之空氣於流至空氣噴射器3 〇〇之水,:: 34 ,丄 111 隨吸進該空氣流入路3 〇 i的空氣之移動,空氣流 路3 〇 1之空氣亦朝向泵7流動。朝向該泵7而 *·動之氣流,將泵7冷卻。因此可將泵7因運作而 發生之熱予以逸散。因此可抑制泵能力之降低。 又如第二十一圖所示,空氣溶解水生成裝置1 宜為進一步具備送氣管1 05。該送氣管i 05具 備.一端,其與空氣釋放閥丄〇 〇之空氣除去孔連 接;及另一端,其插入於固定裴置2〇〇内部。在 此情形,自空氣除去孔所釋放之空氣被輸送至固定 =置2 〇 〇内部。被輸送至固定裝置2 〇 〇内部的 在固定裝置2〇〇内部產生空氣流。藉由該 空氣流而使泵2被冷卻。因此藉由該構成可抑制泵 之成力降低。 接著,上述空氣溶解水生成裝置1係配置於浴 室。第二十三圖係顯示配置於浴室9 5 〇之浴槽9 〇 〇及空氣溶解水生成裝置i。浴槽9 〇 〇係與洗 務場鄰接而設。在浴槽9 〇。之絲場側之緣安裝 外蓋9 〇 1。§亥外盖9 0 1係形成為覆蓋浴槽9 〇 〇之洗滌場侧的面。因此,外蓋9 〇丄係定義為洗 務場與浴槽之境界。外蓋9 0 1在與浴槽外周面之 間形成收納空間9 ◦ 2。接著,空氣溶解水生成& 置1係配置於收納空間。 接著,構成空氣溶解水生成裝置丄之泵7與槽 35 2係設置於循環流路,故倨環流路自一端部之吸進 口 4 0 3吸進浴槽9 0 0内之熱水,自另一端之液 體排h4〇2喷出至浴槽9 ◦◦内,其構成為將 自空亂溶解水生成裝置i之液體流出口所供應之氣 體溶解水自液體排放口 4 〇 2噴出至浴槽内,在浴 槽9 0 0内供給微細氣泡。 ~ 在此情形,宜為在外蓋9 0 1與空氣溶解水生 成裝置之間,或在外蓋9 〇 1之浴槽9 0 ◦側之面 設置防音材料9 〇 3。藉此可防止空氣溶解水生成 裝置1在操作中發出之音漏出外部。 以上所述僅為本發明之較佳可行實施例,非因 此侷限本發明之專㈣護範圍,故舉凡運用本發明 說明書及圖式内容所為之等效技術變化,均包含於 本發明之權利保護範圍内,合予陳明。 【圖式簡單說明】 第一圖係顯示本發明空氣溶解水生成裝置之基 本構造的立體圖。 第二圖係本發日m容解水生成t置基本構造 之側面剖面的概略圖。 第三圖係本發明噴射器之側面剖面的概略圖。 第四圖係顯不本發明空氣溶解水生成裝置之基 本構造的側面剖面圖。 第五圖係本發明空氣溶解水生成裝置側面剖面 36 1361111 的概略圖。 第六圖係本發明實施形態一之槽的一部分之分 • 解立體圖。 • 第七圖係本發明實施形態一之空氣溶解水生成 • 裝置之側面圖。 第八圖係本發明實施形態一之空氣溶解水生成 裝置的第七圖中的A — A側面剖面圖。 第九圖係本發明實施形態一之空氣溶解水生成 裝置之第七圖中的B — B側面剖面圖。 第十圖係本發明實施形態一之空氣溶解水生成 裝置之侧面剖面圖。 第十一圖係本發明實施形態一之空氣溶解水生 成裝置之立體圖。 第十二圖係本發明實施形態一之空氣溶解.·水生 成裝置的背面圖。 • 第十三圖係本發明之實施形態一之槽的一部分 分解立體圖。 第十四圖係本發明實施形態一之空氣釋放閥的 側面剖面圖。 第十五圖係本發明實施形態一之槽下部的一部 • 分分解立體圖。 ' 第十六圖係本發明實施形態一之槽下部的一部 分擴大剖面圖。 第十七圖係顯示改變本發明實施形態一之空氣 37 1361111 >谷解水生成裝置的排氣比率時,溶氧濃度上升樣態 的圖表。 第十八圖係顯不本發明實施形態一之空氣溶解 水生成裝置的排氣比與溶氧濃度上升量之關係圖 表。 第十九圖係本發明實施形態二之空氣溶解水生 成裝置的立體圖。 ’ 第二十圖係本發明實施形態二之空氣溶解水生 成袭置的一部分擴大剖面圖。 · 处〆第一十一圖係本發明實施形態二之變更態様的 空氣溶解水生成裴置之一部分擴大剖面圖。 第一十二圖係顯示本發明實施形態一之空氣溶 解水生成裝置與浴槽關係的模式圖。 第一十二圖係顯不本發明空氣溶解水生成裝置 之在浴室中配置的模式圖。 【主要元件符號說明】 鲁 1空氣溶解水生成裝置 2槽 2 L槽下部 2 U槽上部 3 槽底部 · 4 液體流入口 5 水供給管路 38 1361111 5 1 第一端 6 液體 • 7 泵 • 71 泵入口 72 泵出口 .. 8 液體流出口 8b 液體流出管路 8 c 擋板 β 9管路 1 1水 1 2回流管路 1 3空氣流出口 14空氣流入口 1 6接合部分 1 7喷射器 • 171 第一端 17 2 第二端 1 8氣體 2 0 U,2 0 L 凸緣 2 2混合室 • 2 3分離室 231 第一副分離室 232 第二副分離室 2 3 2 U整流板 1361111 2 6隔壁 2 6 P 連通路 2 6 S 一面 2 6W 傾斜壁 2 9擋板 2 9 L 導板 2 9 P 連通路 2 9 S 相向之一面 2 9 U 延伸板 100 空氣釋放閥 101 汽缸筒 1 0 1 B下面 10 2 浮標 10 3 開口 104 空氣除去孔 10 5 送氣管 200 固定裝置 2 0 1凸緣 300 空氣喷射器 301 空氣流入路 302 空氣供給口 4 0 0,4 0 1 配管 402 液體排放口 403 吸進口 1361111 9 0 0 浴槽 9 0 1外蓋 902 收納空間 903 防音材料 9 5 0 浴室 C 控制器Oxygen concentration_XLi_〇-~ΛΑ,_〇ι ^~λ1^5ι 18. 5 Air release valve 1〇〇 The air exhausted per unit time i: = is determined to be via the water supply line 5 to be mixed The air side V of the air enters the air in the tank 2 by 2% per unit amount to set the gas discharge amount to more than 20% of the gas supply amount, which is fortunate; the nitrogen dissolves more in water solubility. The amount of oxygen in the liquid 5 is increased. Therefore, it is possible to generate a liquid having a sufficiently high dissolved oxygen concentration, and a specific means and method for introducing the amount of exhaust gas of the gas due to the air release valve i 导入 into the dissolution tank 2 by 2% or more of the air supply amount can be exemplified. Increase the amount of gas extracted by the gas introduction injector 3 〇33 1361111. Further, the same effect can be obtained by adjusting the shape and area of the opening of the gas removing port 35 in the air release valve ^ Q 〇. Then, the same effect can be obtained by appropriately selecting the features. Furthermore, the same effect can be obtained by combining these features. (Embodiment 2) Figs. 19 and 20 show perspective views of an air-dissolved water generating apparatus 1 according to Embodiment 1 of the present invention. In the same manner as in the first embodiment, the same reference numerals will be given to the same components, and the same configuration 2 will be omitted. The air-dissolved water generating apparatus 1 of the present embodiment includes: a tank 2, a pump 7, a return line 1, 2. an ejector 丄7 straight line 5 (not shown), a liquid outflow line 8b, and an air release valve. 1 0 0, air ejector 3 〇〇 and air inflow: 『 I 〇 义 喷射 3 3 0 0 is installed in the pump inlet 1 of the pump 7. An air supply is provided at one end of the air ejector 3 ’ , and the other end is inserted into the inside of the fixing device 2 〇 在 on the back side of the upper end of the |7 periphery. Then, the system is configured to transport the sucked air through the inflow path 30 于 to the water spray: water of 3000. Therefore, the water in the day and mouth chamber 2 2 can be premixed. Thereby, it is possible to obtain an air-dissolved water generating device 1 which is configured to efficiently produce two dissolved water. The body is also configured to flow into the air ejector 3 through the air that has been sucked in by the air stream (3):: 34, 丄111 is drawn into the air of the air inflow path 3 〇i As it moves, the air of the air flow path 3 〇1 also flows toward the pump 7. The pump 7 is cooled toward the pump 7 and the moving air. Therefore, the heat generated by the pump 7 due to operation can be dissipated. Therefore, the reduction in pump capacity can be suppressed. Further, as shown in the twenty-first embodiment, the air-dissolved water generating device 1 is preferably further provided with an air supply pipe 105. The air supply pipe i 05 has one end which is connected to the air removing hole of the air release valve ;, and the other end which is inserted inside the fixed cymbal 2 。. In this case, the air released from the air removal hole is sent to the inside of the fixed = set 2 〇 。. It is conveyed to the inside of the fixture 2 〇 产生 Air flow is generated inside the fixture 2〇〇. The pump 2 is cooled by this air flow. Therefore, with this configuration, the decrease in the force of the pump can be suppressed. Next, the above-described air-dissolved water generating device 1 is placed in a bath. The twenty-third figure shows the bath 9 〇 and the air-dissolved water generating device i disposed in the bathroom. The bath 9 〇 is adjacent to the wash yard. In the bath 9 〇. The edge of the wire side is installed. Cover 9 〇 1. § The outer cover 901 is formed to cover the surface of the washing tank side of the bath 9 〇 。. Therefore, the outer cover 9 is defined as the boundary between the wash yard and the bath. The outer cover 902 forms a storage space 9 ◦ 2 between the outer peripheral surface of the bathtub. Next, the air-dissolved water generation & 1 is placed in the storage space. Then, the pump 7 and the groove 35 2 constituting the air-dissolved water generating device are disposed in the circulation flow path, so that the ring-shaped flow path is sucked into the hot water in the bath 90 from the suction inlet 4 0 3 at one end, from the other end. The liquid discharge port h4〇2 is ejected into the bath 9 ,, and is configured to eject the gas dissolved water supplied from the liquid outflow port of the air-dissolved water generating device i from the liquid discharge port 4 〇 2 into the bath. Fine bubbles are supplied in the bath 90000. ~ In this case, it is preferable to provide the soundproof material 9 〇 3 between the outer cover 910 and the air-dissolved water generating device, or on the side of the bath 90 side of the outer cover 9 〇 1 . Thereby, it is possible to prevent the sound emitted from the air-dissolved water generating device 1 from leaking out of the outside during operation. The above description is only a preferred embodiment of the present invention, and is not intended to limit the scope of the invention. Therefore, the equivalent technical changes of the present invention and the contents of the drawings are included in the protection of the present invention. Within the scope, it is combined with Chen Ming. BRIEF DESCRIPTION OF THE DRAWINGS The first drawing shows a perspective view of a basic structure of an air-dissolved water generating apparatus of the present invention. The second figure is a schematic view of a side cross section of the basic structure of the water-forming water formation in the present day. The third drawing is a schematic view of a side cross section of the injector of the present invention. The fourth figure is a side cross-sectional view showing the basic structure of the air-dissolved water generating apparatus of the present invention. Fig. 5 is a schematic view showing a side section 36 1361111 of the air-dissolved water generating apparatus of the present invention. Fig. 6 is a perspective view of a part of the groove of the first embodiment of the present invention. • Fig. 7 is a side view showing the apparatus for generating dissolved air in the first embodiment of the present invention. Figure 8 is a side cross-sectional view taken along line A - A of the seventh diagram of the air-dissolved water generating apparatus according to the first embodiment of the present invention. Figure 9 is a side cross-sectional view taken along the line B-B in the seventh diagram of the air-dissolved water generating apparatus according to the first embodiment of the present invention. Figure 11 is a side cross-sectional view showing an air-dissolved water generating apparatus according to Embodiment 1 of the present invention. Fig. 11 is a perspective view showing the air-dissolved water producing apparatus of the first embodiment of the present invention. Fig. 12 is a rear view showing the air-dissolving apparatus of the first embodiment of the present invention. Fig. 13 is an exploded perspective view showing a part of the groove of the first embodiment of the present invention. Fig. 14 is a side sectional view showing the air release valve of the first embodiment of the present invention. The fifteenth embodiment is a partial exploded perspective view of the lower portion of the tank according to the first embodiment of the present invention. Fig. 16 is a partially enlarged sectional view showing the lower portion of the groove in the first embodiment of the present invention. Fig. 17 is a graph showing a state in which the dissolved oxygen concentration is increased when the exhaust ratio of the air 37 1361111 > glutathion water generating apparatus according to the first embodiment of the present invention is changed. Fig. 18 is a graph showing the relationship between the exhaust ratio of the air-dissolved water generating apparatus and the amount of increase in dissolved oxygen concentration in the first embodiment of the present invention. Fig. 19 is a perspective view showing the air-dissolved water producing apparatus of the second embodiment of the present invention. Fig. 20 is a partially enlarged cross-sectional view showing the air-dissolved aquatic growth apparatus according to the second embodiment of the present invention. In the eleventh embodiment, a partially enlarged cross-sectional view of the air-dissolved water generating device in the modified state of the second embodiment of the present invention is shown. Fig. 12 is a schematic view showing the relationship between the air-dissolved water generating apparatus and the bath in the first embodiment of the present invention. The twelfth figure shows a schematic view of the arrangement of the air-dissolved water generating device of the present invention in a bathroom. [Main component symbol description] Lu 1 air dissolved water generator 2 tank 2 L tank lower 2 U tank upper 3 tank bottom · 4 Liquid inlet 5 Water supply line 38 1361111 5 1 First end 6 Liquid • 7 Pump • 71 Pump inlet 72 Pump outlet: 8 Liquid outflow 8b Liquid outflow line 8 c Baffle β 9 Line 1 1 Water 1 2 Return line 1 3 Air flow outlet 14 Air flow inlet 1 6 Engagement section 1 7 Ejector • 171 First end 17 2 Second end 1 8 gas 2 0 U, 2 0 L Flange 2 2 Mixing chamber • 2 3 Separation chamber 231 First sub-separation chamber 232 Second sub-separation chamber 2 3 2 U rectifying plate 1361111 2 6 partition 2 6 P connection 2 6 S side 2 6W inclined wall 2 9 baffle 2 9 L guide 2 9 P connection 2 9 S facing one face 2 9 U extension plate 100 air release valve 101 cylinder tube 1 0 1 B below 10 2 buoy 10 3 opening 104 air removal hole 10 5 air supply pipe 200 fixing device 2 0 1 flange 300 air injector 301 air inflow path 302 air supply port 4 0 0, 4 0 1 pipe 402 liquid discharge port 403 suction Import 1361111 9 0 0 Bath 9 0 1 Cover 902 Storage space 903 Soundproof material 9 5 0 Bathroom C controller
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JP6010893B2 (en) * | 2011-10-27 | 2016-10-19 | 大日本印刷株式会社 | Water filling method, water filling system, and water filling bottle |
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JP5887555B2 (en) * | 2012-03-08 | 2016-03-16 | パナソニックIpマネジメント株式会社 | Gas dissolution tank |
JP5870262B2 (en) * | 2012-03-08 | 2016-02-24 | パナソニックIpマネジメント株式会社 | Gas dissolution tank |
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Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04338297A (en) * | 1991-05-15 | 1992-11-25 | Matsushita Electric Ind Co Ltd | Water purifying device |
JP2663329B2 (en) * | 1993-09-01 | 1997-10-15 | 和泉電気株式会社 | Excess gas separation type gas-liquid pressurized reactor |
JP2792016B2 (en) * | 1994-05-31 | 1998-08-27 | 和泉電気株式会社 | Gas-liquid dissolving and mixing equipment |
JPH10192867A (en) * | 1996-12-27 | 1998-07-28 | Ngk Spark Plug Co Ltd | Ozone water maker |
JP3887900B2 (en) * | 1997-08-29 | 2007-02-28 | 松下電器産業株式会社 | Gas dissolving apparatus and shower apparatus using the same |
JP2000263038A (en) * | 1999-03-15 | 2000-09-26 | Matsushita Electric Ind Co Ltd | Floatation equipment and circulation warm bath apparatus |
JP2001121168A (en) * | 1999-08-18 | 2001-05-08 | Yaskawa Electric Corp | Water treating apparatus |
JP2004283810A (en) * | 2003-01-28 | 2004-10-14 | Matsushita Electric Works Ltd | Structure of dissolution tank and fine air bubble generator equipped with the dissolution tank |
JP2004313905A (en) * | 2003-04-15 | 2004-11-11 | Matsushita Electric Works Ltd | Structure of gas-liquid dissolving tank |
JP4581556B2 (en) * | 2003-08-25 | 2010-11-17 | パナソニック電工株式会社 | Gas-liquid dissolution tank |
JP4007295B2 (en) * | 2003-09-24 | 2007-11-14 | 松下電工株式会社 | Bubble generation bathtub |
JP4168926B2 (en) * | 2003-12-19 | 2008-10-22 | 松下電工株式会社 | Bathtub with fine bubble generator |
JP2005270338A (en) * | 2004-03-24 | 2005-10-06 | Matsushita Electric Works Ltd | Air-liquid dissolving tank for bubble generating bathtub |
JP2006035175A (en) * | 2004-07-29 | 2006-02-09 | Sanyo Electric Co Ltd | Bath water cleaner |
-
2009
- 2009-08-25 KR KR1020117005755A patent/KR101250362B1/en active IP Right Grant
- 2009-08-25 WO PCT/JP2009/064792 patent/WO2010024253A1/en active Application Filing
- 2009-08-25 CN CN200980133192.0A patent/CN102131572B/en active Active
- 2009-08-26 TW TW098128660A patent/TW201008657A/en unknown
Also Published As
Publication number | Publication date |
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WO2010024253A1 (en) | 2010-03-04 |
CN102131572B (en) | 2014-01-08 |
KR20110043755A (en) | 2011-04-27 |
KR101250362B1 (en) | 2013-04-09 |
CN102131572A (en) | 2011-07-20 |
TW201008657A (en) | 2010-03-01 |
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