TW201102457A - Method and apparatus for producing high concentration hypochloric acid sterilization water - Google Patents

Method and apparatus for producing high concentration hypochloric acid sterilization water Download PDF

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TW201102457A
TW201102457A TW98123707A TW98123707A TW201102457A TW 201102457 A TW201102457 A TW 201102457A TW 98123707 A TW98123707 A TW 98123707A TW 98123707 A TW98123707 A TW 98123707A TW 201102457 A TW201102457 A TW 201102457A
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chlorine
electrode
electrolysis
anode
containing electrolyte
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TW98123707A
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Chinese (zh)
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TWI427189B (en
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Wei Fang
Shi-Wei Kong
Ming-Yih Chang
Chi-Yu Chuang
Lin-Chi Chen
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Wei Fang
Shi-Wei Kong
Ming-Yih Chang
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Abstract

The invention provides a method for batchly or continuously producing high concentration hypochloric acid sterilization water through diaphragm free electrolysis manner in a first stage and an acid-base adjustment manner in a second stage. The electrolysis manner in the first stage uses a diaphragm free electrolysis device to electrolyze a chlorine-containing electrolyte solution to prepare alkali electrolyte water. The acid-base regulation manner in the second stage electrolyzes alkali electrolytic water prepared by the diaphragm free electrolysis device in an anode side electrolysis bath by using a diaphragm electrolysis device. Alternatively, pH value of the alkali electrolytic water is regulated by cation exchange manner so that pH value falls within a range between 5.5 and 6.5.

Description

201102457 六、發明說明: 【發明所屬之技術領域】 本發明係關於次氯酸滅菌水之製造方法,尤其是以兩 階段電解方式製造高濃度次氯酸滅菌水之方法。本發明亦 關於次氯酸滅菌水之製造裝置。 【先前技術】 已知次氯酸具有良好的滅菌能力,且可簡單地以電解 含氯電解質溶液的方式製得。例如本國專利公告第301644 I 號,傳統上使用無隔膜電解裝置電解含氯電解質溶液,製 備具有滅菌能力的次氯酸水。惟,以無隔膜電解裝置電解 生成的電解水通常呈弱鹼性。又’次氯酸濃度與pH値有 關,且pH値在5.5〜6.5的範圍時,次氯酸濃度最高可達 10 0%。因此,爲了提高次氯酸濃度,以無隔膜電解裝置製 備的鹼性電解水需要額外地添加酸’以降低pH値。 【發明内容】 本發明之目的在於提供高濃度次氯酸滅菌水之製造方 法,透過兩段式電解方式將鹼性電解水調和成酸性電解 I 水,無須透過額外添加酸之步驟’即可製成高濃度次氯酸 滅菌水。 本發明之另一目的在於提供高濃度次氯酸滅菌水之製 造裝置,其適用於以兩段式電解方式製造高濃度次氯酸滅 菌水。 本發明之另一目的在於提供高濃度次氯酸滅菌水之製 造方法,透過第一階段的無隔膜電解方式及第二階段的陽 離子交換方式,將電解水調和成酸性電解水’無須透過額 201102457 外添加酸之步驟,即可製成高濃度次氯酸滅菌水。 根據本發明,高濃度次氯酸滅菌水係批次或連續製造 本發明所屬技術領域中具有通常知識者,在閱讀此說 明書之後,將可理解本發明其他目的及優點。 【實施方式】 參照第1圖,第1圖顯示根據本發明第1實施例之高 濃度次氯酸滅菌水之製造裝置,整體以元件符號10標示。 高濃度次氯酸滅菌水之製造裝置10包含包含無隔膜 電解裝置12及隔膜電解裝置14。 無隔膜電解裝置12係配置有陽極20及陰極22。隔膜 電解裝置14包含以隔膜28分隔的陽極側電解槽18及陰極 側電解槽16。於該陽極側電解槽18中配置有陽極26,於 該陰極側電解槽16中配置有陰極24。 無隔膜電解裝置12係與隔膜電解裝置14串接並配置 於隔膜電解裝置14之上游,使得無隔膜電解裝置12製備 的鹼性電解水可自動地導引至隔膜電解裝置14之陽極側 電解槽18。 接著’將參照第1圖所示之高濃度次氯酸滅菌水之製 造裝置10說明根據本發明之高濃度次氯酸滅菌水之製造 方法。 本發明之特點在於兩段式的電解方式,由無隔膜電解 裝置12進行第1階段的電解反應以製備鹼性電解水,由隔 膜電解裝置14進行第2階段的電解反應以調整鹼性電解水 之pH値’使得pH値落在能提高次氯酸濃度之範圍。 將含氯電解質溶液,例如氯化鈉溶液,包括過飽和、 -4- I S3 201102457 飽和或未飽和食鹽水、海水、滷水或生理食鹽水等’注入 於無隔膜電解裝置12»作爲含氯電解質並不以氯化鈉爲 限,鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽類同樣可 應用於製造次氯酸滅菌水。 先以無隔膜電解裝置12電解氯化鈉溶液。在此第1階 段的電解過程中,在陽極20處,水H20釋出電子e_產生 氧氣〇2及氫離子H+,同時氯離子(:1_釋出電子^產生氯氣 Cl2。氯氣Cl2溶於電解槽10中的氯化鈉溶液,因而在無隔 膜電解裝置12產生鹽酸HC1、次氯酸HC10及次氯酸鈉 NaCIO。在陰極22處,水H20接收電子e·產生氫氣心及 氫氧離子OH_。氫氧離子OH·又與鈉離子Na +結合產生氫氧 化鈉NaO Η。持續第1階段的電解反應,直到電解水中自由 氯(Free Active Chlorine,FAC)達預定濃度爲止。此時,以 無隔膜電解裝置12電解生成的電解水會呈現鹼性或弱鹼 性。 應瞭解的是,文中所稱的自由氯係指次氯酸HOC1、次 氯酸根離子ocr及氯氣Cl2三者之總和。 將以無隔膜電解裝置12電解生成的電解水導引至隔 膜電解裝置14之陽極側電解槽18,而膜電解裝置14之陰 極側電解槽16則收容有電解質溶液。 接著以隔膜電解裝置14進行第2階段的電解反應。在 此第2階段的電解過程中,在陽極側電解槽18之陽極處, 水HW釋出電子^產生氧氣〇2及氫離子H+,同時氯離子 C1'釋出電子e·產生氯氣C12,使得陽極側電解槽18的氫離 子H +濃度會逐漸升高,FAC也逐漸增加。第2階段的電解 201102457 反應進行預定時間,使得pH値落在5·5〜6.5的範圍。 第2圖顯示根據本發明第2實施例之高濃度次氯酸滅 菌水之製造裝置,整體以元件符號40標示。 高濃度次氯酸滅菌水之製造裝置40包含三極式有隔 膜電解裝置42及切換裝置44。 三極式有隔膜電解裝置42包含以隔膜52分隔的陽極 側電解槽46及陰極側電解槽48。 第1電解槽46係配置有第1電極54及第2電極56, 而第2電解槽48係配置有第3電極58。 切換裝置44係用於改變該等電極的極性配置。較佳 地,第1電極5 4係恆常地或可控制地作用成陽極,而藉由 切換裝置44之切換,第2及第3電極56、58之其中一者 作用成陰極,而另一者則閒置。 當第2電極56作用成陰極時,配合作用成陽極的第1 電極54,第1電解槽46係作用成無隔膜電解裝置,用於 進行第1階段的電解反應,此時第3電極58爲閒置。當第 3電極58作用成陰極時’配合作用成陽極的第丨電極54, 第1電解槽46及第2電解槽48係作用成隔膜電解裝置’ 用於進行第2階段的電解反應,此時第2電極56爲閒置。 關於第1階段及第2階段的電解反應,原理與前述實施例 相同,故省略其說明。 本發明之第3實施例係顯示於第3圖,可藉由在第2 電解槽48中配置第4電極60而將三極式有隔膜電解裝置 修改成四極式有隔膜電解裝置。當第1電極54及第2電極 之一者作用成陰極且第1電極54及第2電極56之另一 201102457 者作用成陽極時’第1電解槽46係作用成無隔膜電解裝 置’用於進行第1階段的電解反應。當第3電極58及/或 第4電極60作用成陰極且第1電極54及/或第2電極56 作用成陽極時,第1電解槽46及第2電解槽48係作用成 隔膜電解裝置,用於進行第2階段的電解反應。 於另一替代方式中’當第3電極58及第4電極60之 —者作用成陰極且第3電極58及第4電極60之另一者作 用成陽極時,第2電解槽48係作用成無隔膜電解裝置,用 φ 於進行第1階段的電解反應。當第3電極58及/或第4電 極60作用成陽極且第1電極54及/或第2電極56作用成 陰極時’第1電解槽46及第2電解槽48係作用成隔膜電 解裝置’用於進行第2階段的電解反應。關於第〖階段及 第2階段的電解反應,原理與前述實施例相同,故省略其 說明。 在第2圖及第3圖所示實施例中,藉由改變電極的極 性配置,即可在單一的三極式或四極式有隔膜電解裝置中 φ 完成兩階段的電解反應》 根據本發明,酸鹼調整並不以利用隔膜電解裝置進行 的電解反應爲限’亦可在第1階段的電解反應後,將經第 1階段電解反應產生的電解水導引通過陽離子交換樹脂。 由於存在於電解水中的鈉離子與陽離子交換樹脂之氫離子 之間的交換’流過陽離子交換樹脂的電解水之pH値會降 低,藉以將pH値調整在5.5〜6.5的範圍》 第4圖顯示根據本發明第4實施例之高濃度次氯酸滅 菌水之製造裝置,整體以元件符號30標示。 201102457 高濃度次氯酸滅菌水之製造裝置30包含過濾器32、 兩個無隔膜電解裝置34及離子交換器36。待處理的原水 經由過濾器32淨化後,連續地流經兩個無隔膜電解裝置 34並被電解成鹼性電解水。接著,鹼性電解水流經收容有 陽離子交換樹脂的離子交換器36而調整成酸性電解水,尤 其是pH値調在5·5~6·5範圍的酸性電解水。可在待處理的 原水流經過濾器32之前或之後,添加含氯電解質。電解水 的流率、無隔膜電解裝置的數量及陽離子交換樹脂的含量 ^ 可依需求而調整。 雖然本發明參照較佳實施例而進行說明示範,惟應了 解的是在不脫離本發明之精神及範疇內,對於本發明所屬 技術領域中具有通常知識者而言,仍得有許多變化及修 改。因此’本發明並不限制於所揭露的實施例,而是以後 附申請專利範圍之文字記載爲準,即不偏離本發明申請專 利範圍所爲之均等變化與修飾,應仍屬本發明之涵蓋範圍。 【圖式簡單說明】 φ 第1圖顯示根據本發明之高濃度次氯酸滅菌水之製造 裝置之實施例; 第2圖顯示根據本發明之高濃度次氯酸滅菌水之製造 裝置之第2實施例’其中採用三極式有隔膜電解裝置; 第3圖顯示根據本發明之高濃度次氯酸滅菌水之製造 裝置之第3實施例’其中採用四極式有隔膜電解裝置;及 第4圖顯示根據本發明之高濃度次氯酸滅菌水之製造 裝置之第4實施例,其中採用離子交換器。 201102457 【主要元件符號說明】 ' ίο 高濃度次氯酸滅菌水之製造裝置 12 無隔膜電解裝置 14 隔膜電解裝置 18 陽極側電解槽 16 陰極側電解槽 2 0 陽極 22 陰極 24 陽極 鲁26陰極 28 隔膜 30 高濃度次氯酸滅菌水之製造裝置 32 過濾器 34 無隔膜電解裝置 36 離子交換器 40 高濃度次氯酸滅菌水之製造裝置 I 42 三極式有隔膜電解裝置42 44 切換裝置 46 陽極側電解槽 48 陰極側電解槽 52 隔膜5 2 54 第1電極 56 第2電極 5 8 第3電極 60 第4電極 [S3201102457 VI. Description of the Invention: [Technical Field] The present invention relates to a method for producing hypochloric acid sterilized water, and more particularly to a method for producing high-concentration hypochlorite sterilized water by a two-stage electrolysis method. The present invention also relates to a manufacturing apparatus for hypochloric acid sterilized water. [Prior Art] Hypochlorous acid is known to have good sterilization ability, and can be simply obtained by electrolyzing a chlorine-containing electrolyte solution. For example, National Patent Publication No. 301644 I conventionally uses a non-diaphragm electrolysis apparatus to electrolyze a chlorine-containing electrolyte solution to prepare hypochlorous acid water having a sterilizing ability. However, electrolyzed water produced by electrolysis without a diaphragm electrolysis device is generally weakly alkaline. Further, the concentration of hypochlorous acid is related to pH ,, and the pH is in the range of 5.5 to 6.5, and the hypochlorous acid concentration is up to 100%. Therefore, in order to increase the hypochlorous acid concentration, the alkaline electrolyzed water prepared by the diaphragmless electrolysis apparatus requires an additional addition of acid to lower the pH. SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a high concentration of hypochloric acid sterilized water, which is prepared by a two-stage electrolysis method to adjust an alkaline electrolyzed water into an acidic electrolyzed water without the step of adding an additional acid. A high concentration of hypochlorous acid sterilized water. Another object of the present invention is to provide a high concentration hypochloric acid sterilized water manufacturing apparatus which is suitable for producing high concentration hypochlorous acid sterilizing water by two-stage electrolysis. Another object of the present invention is to provide a method for producing high-concentration hypochlorite sterilized water, which is prepared by a first-stage non-diaphragm electrolysis method and a second-stage cation exchange method to reconcile electrolyzed water into an acidic electrolyzed water without a permeation amount 201102457 A high concentration of hypochloric acid sterilized water can be prepared by externally adding an acid. In accordance with the present invention, a high concentration of hypochlorite sterilized water batch or continuous manufacturing will be understood by those of ordinary skill in the art to which this invention pertains. [Embodiment] Referring to Fig. 1, there is shown a manufacturing apparatus for high-concentration hypochlorite sterilized water according to a first embodiment of the present invention, which is denoted by the reference numeral 10. The apparatus 10 for producing high-concentration hypochlorite sterilized water includes a separator-free electrolysis device 12 and a diaphragm electrolysis device 14. The diaphragmless electrolysis device 12 is provided with an anode 20 and a cathode 22. The diaphragm electrolysis device 14 includes an anode side electrolytic cell 18 and a cathode side electrolytic cell 16 separated by a separator 28. An anode 26 is disposed in the anode side electrolytic cell 18, and a cathode 24 is disposed in the cathode side electrolytic cell 16. The diaphragmless electrolysis device 12 is connected in series with the diaphragm electrolysis device 14 and disposed upstream of the diaphragm electrolysis device 14, so that the alkaline electrolyzed water prepared by the diaphragmless electrolysis device 12 can be automatically guided to the anode side electrolysis cell of the diaphragm electrolysis device 14. 18. Next, a manufacturing method of high-concentration hypochlorite sterilized water according to the present invention will be described with reference to a manufacturing apparatus 10 for high-concentration hypochlorite sterilized water shown in Fig. 1. The present invention is characterized by a two-stage electrolysis method in which the electrolysis reaction in the first stage is performed by the diaphragmless electrolysis device 12 to prepare alkaline electrolyzed water, and the electrolysis reaction in the second stage is performed by the diaphragm electrolysis device 14 to adjust the alkaline electrolyzed water. The pH 値' causes the pH to fall within a range that increases the concentration of hypochlorous acid. Injecting a chlorine-containing electrolyte solution, such as a sodium chloride solution, including supersaturated, -4-I S3 201102457 saturated or unsaturated brine, seawater, brine or physiological saline, into the membrane-free electrolysis device 12» as a chlorine-containing electrolyte Not limited to sodium chloride, alkali metal chlorides, alkaline earth metal chlorides or chlorine-containing salts are also applicable to the manufacture of hypochlorite sterilized water. The sodium chloride solution is first electrolyzed by the diaphragmless electrolysis device 12. In the electrolysis process of the first stage, at the anode 20, the water H20 releases electrons e_ to generate oxygen 〇2 and hydrogen ions H+, while the chloride ions (:1_ liberate electrons generate chlorine gas Cl2. chlorine gas Cl2 dissolves The sodium chloride solution in the electrolytic cell 10 thus produces hydrochloric acid HC1, hypochlorous acid HC10 and sodium hypochlorite NaCIO in the diaphragmless electrolysis device 12. At the cathode 22, the water H20 receives electrons e. generates hydrogen gas and hydrogen ions OH_. The oxygen ion OH is combined with the sodium ion Na + to produce sodium hydroxide NaO Η. The first stage of the electrolysis reaction is continued until the free chlorine (FAC) in the electrolyzed water reaches a predetermined concentration. The electrolyzed water produced by electrolysis of device 12 will be alkaline or weakly alkaline. It should be understood that the free chlorine referred to herein refers to the sum of hypochlorite HOC1, hypochlorite ion ocr and chlorine Cl2. The electrolyzed water electrolyzed by the diaphragm electrolysis device 12 is guided to the anode side electrolysis cell 18 of the diaphragm electrolysis device 14, and the cathode side electrolysis cell 16 of the membrane electrolysis device 14 houses the electrolyte solution. Next, the diaphragm electrolysis device 14 performs the second stage. In the electrolysis process of the second stage, at the anode of the anode side electrolytic cell 18, the water HW releases electrons to generate oxygen 〇 2 and hydrogen ions H+, while the chloride ion C1 ' releases electrons e· The chlorine gas C12 causes the hydrogen ion H + concentration of the anode side electrolytic cell 18 to gradually increase, and the FAC gradually increases. The second stage electrolysis 201102457 reacts for a predetermined time, so that the pH falls within the range of 5. 5 to 6.5. 2 is a view showing a manufacturing apparatus for high-concentration hypochlorite sterilized water according to a second embodiment of the present invention, which is denoted by the reference numeral 40. The high-concentration hypochloric acid sterilized water manufacturing apparatus 40 includes a three-electrode type diaphragm electrolysis apparatus 42 and The switching device 44. The three-electrode diaphragm electrolysis device 42 includes an anode side electrolytic cell 46 and a cathode side electrolytic cell 48 separated by a separator 52. The first electrolytic cell 46 is provided with a first electrode 54 and a second electrode 56, and 2 The electrolytic cell 48 is provided with a third electrode 58. The switching device 44 is for changing the polarity arrangement of the electrodes. Preferably, the first electrode 54 is constantly or controllably acted as an anode. Switching device 44 switching, second and third electrodes One of 56, 58 acts as a cathode while the other is idle. When the second electrode 56 acts as a cathode, it cooperates with the first electrode 54 acting as an anode, and the first electrolytic cell 46 acts as a diaphragmless electrolysis device. For performing the first-stage electrolysis reaction, the third electrode 58 is idle at this time. When the third electrode 58 acts as a cathode, 'the second electrode 54 that functions as an anode, the first electrolytic cell 46 and the second electrolytic cell The 48-series acts as a diaphragm electrolyzer "for performing the second-stage electrolysis reaction, and the second electrode 56 is left idle. The principle of the electrolysis reaction in the first stage and the second stage is the same as that of the above embodiment, and the description thereof will be omitted. The third embodiment of the present invention is shown in Fig. 3. The three-electrode diaphragm electrolysis device can be modified into a four-electrode diaphragm electrolysis device by disposing the fourth electrode 60 in the second electrolytic cell 48. When one of the first electrode 54 and the second electrode acts as a cathode and the other electrode 102102457 of the first electrode 54 and the second electrode 56 acts as an anode, the first electrolytic cell 46 acts as a diaphragmless electrolysis device for The first stage of the electrolysis reaction is carried out. When the third electrode 58 and/or the fourth electrode 60 act as a cathode and the first electrode 54 and/or the second electrode 56 act as an anode, the first electrolytic cell 46 and the second electrolytic cell 48 act as a diaphragm electrolysis device. Used to carry out the second stage of the electrolysis reaction. In another alternative, when the third electrode 58 and the fourth electrode 60 act as a cathode and the other of the third electrode 58 and the fourth electrode 60 acts as an anode, the second electrolytic cell 48 acts as a cathode. In the diaphragmless electrolysis apparatus, φ is used to carry out the first-stage electrolysis reaction. When the third electrode 58 and/or the fourth electrode 60 act as an anode and the first electrode 54 and/or the second electrode 56 act as a cathode, the first electrolytic cell 46 and the second electrolytic cell 48 act as a diaphragm electrolyzer. Used to carry out the second stage of the electrolysis reaction. Regarding the electrolysis reactions of the first stage and the second stage, the principle is the same as that of the foregoing embodiment, and the description thereof will be omitted. In the embodiments shown in Figures 2 and 3, by changing the polarity configuration of the electrodes, a two-stage electrolytic reaction can be completed in a single three- or four-pole diaphragm electrolyzer. According to the present invention, The acid-base adjustment is not limited to the electrolytic reaction by the diaphragm electrolysis device. The electrolyzed water produced by the first-stage electrolysis reaction may be guided through the cation exchange resin after the first-stage electrolysis reaction. Due to the exchange between the sodium ions present in the electrolyzed water and the hydrogen ions of the cation exchange resin, the pH of the electrolyzed water flowing through the cation exchange resin is lowered, thereby adjusting the pH 在 in the range of 5.5 to 6.5. The apparatus for producing high-concentration hypochlorite sterilized water according to the fourth embodiment of the present invention is denoted by the reference numeral 30 as a whole. 201102457 The high-density hypochloric acid sterilized water manufacturing apparatus 30 includes a filter 32, two diaphragmless electrolysis devices 34, and an ion exchanger 36. The raw water to be treated is purified by the filter 32, continuously flows through the two diaphragmless electrolysis devices 34, and is electrolyzed into alkaline electrolyzed water. Next, the alkaline electrolyzed water is passed through an ion exchanger 36 containing a cation exchange resin to be adjusted into acidic electrolyzed water, particularly acidic electrolyzed water having a pH of 5·5 to 6·5. A chlorine-containing electrolyte may be added before or after the raw water to be treated flows through the filter 32. The flow rate of the electrolyzed water, the number of non-diaphragm electrolyzers, and the content of the cation exchange resin can be adjusted as needed. While the invention has been described with respect to the preferred embodiments of the present invention, it is understood that many changes and modifications may be made to those of ordinary skill in the art to which the invention pertains, without departing from the spirit and scope of the invention. . Therefore, the invention is not limited to the disclosed embodiments, but is intended to be included in the scope of the appended claims. range. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 shows an embodiment of a manufacturing apparatus for high-concentration hypochlorite sterilized water according to the present invention; and FIG. 2 shows a second manufacturing apparatus of high-concentration hypochlorite sterilized water according to the present invention. Embodiment 3 wherein a three-electrode diaphragm electrolysis device is employed; FIG. 3 shows a third embodiment of a manufacturing apparatus for high-concentration hypochlorite sterilized water according to the present invention, wherein a four-electrode diaphragm electrolysis device is employed; and FIG. 4 A fourth embodiment of a manufacturing apparatus for high-concentration hypochlorite sterilized water according to the present invention is shown in which an ion exchanger is employed. 201102457 [Explanation of main component symbols] ' ίο High-density hypochloric acid sterilized water manufacturing equipment 12 Non-diaphragm electrolysis device 14 Diaphragm electrolysis device 18 Anode side electrolysis cell 16 Cathode side electrolysis cell 2 0 Anode 22 Cathode 24 Anode Lu 26 Cathode 28 Separator 30 High-density hypochlorite sterilized water manufacturing equipment 32 Filter 34 Non-diaphragm electrolysis unit 36 Ion exchanger 40 High-concentration hypochlorous acid sterilized water manufacturing apparatus I 42 Three-pole type diaphragm electrolysis unit 42 44 Switching unit 46 Anode side Electrolyzer 48 Cathode side electrolytic cell 52 Separator 5 2 54 First electrode 56 Second electrode 5 8 Third electrode 60 Fourth electrode [S3

Claims (1)

201102457 七、申請專利範圍: 1. 一種高濃度次氯酸滅菌水之製造方法’其包含下列步驟: 9 提供一無隔膜電解裝置,於其中配置有陽極及陰極; 提供一隔膜電解裝置,其包含以隔膜分隔的陽極側電 解槽及陰極側電解槽’於該陽極側電解槽中配置有陽 極,於該陰極側電解槽中配置有陰極且收容有導電性電 解質溶液: 藉由該無隔膜電解裝置電解含氯電解質溶液以製備鹼 性電解水; 將該鹼性電解水導引至該隔膜電解裝置之陽極側電解 槽; 藉由該隔膜電解裝置電解該鹼性電解水一預設時間, 以將該鹼性電解水之pH値調整在5. 5〜6.5的範圍,藉以 製造高濃度次氯酸滅菌水。 2. 如申請專利範圍第1項之製造方法,其中電解含氯電解 質溶液以製備鹼性電解水之步驟係持續直到該鹼性電解 φ 水中自由氯達一預定濃度爲止。 3. 如申請專利範圍第1或2項之製造方法,其中該含氯的 電解質包含鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽 類。 4_如申請專利範圍第1或2項之製造方法,其中在該含氯 電解質溶液之溶質爲氯化鈉的情況下,該含氯電解質溶 液包括過飽和、飽和或未飽和食鹽水、海水、滷水或生 理食鹽水。 5. —種高濃度次氯酸滅菌水之製造方法,其包含下列步驟: [S] -10- 201102457 提供多極式有隔膜電解裝置,其包含以隔膜分隔的第1 電解槽及第2電解槽,該第1電解槽係配置有第1電極 及第2電極,該第2電解槽係配置有至少第3電極且收 容有導電性電解質溶液’該第1電極係恆常地或可可控 制地作用成陽極’而該2及3電極可切換地作用成陽極 或陰極; 藉由作用成陽極的第1電極及作用成陰極的第2電極 電解該第1電解槽中的含氯電解質溶液以製備鹼性電解 藉由作用成陽極的第1電極及作用成陰極的第3電極 電解該第1電解槽中的該鹼性電解水一預設時間,以將 該鹼性電解水之pH値調整在5.5〜6.5的範圍,藉以製造 高濃度次氯酸滅菌水。 6.如申請專利範圍第5項之製造方法,其中電解該第1電 解槽中的含氯電解質溶液以製備鹼性電解水之步驟係持 續直到該鹼性電解水中自由氯達一預定濃度爲止; φ 7·如申請專利範圍第5或6項之製造方法,其中該含氯的 電解質包含鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽 類》 8. 如申請專利範圍第5或6項之製造方法,其中在該含氯 電解質溶液之溶質爲氯化鈉的情況下,該含氯電解質溶 液包括過飽和、飽和或未飽和食鹽水、海水、滷水或生 理食鹽水。 9. 一種高濃度次氯酸滅菌水之製造方法,其包含下列步驟: 提供一無隔膜電解裝置,於其中配置有陽極及陰極; [S3 -11 - 201102457 提供一離子交換器,其收容有陽離子交換樹脂; 藉由該無隔膜電解裝置電解含氯電解質溶液以製備鹼 性電解水; 藉由將該鹼性電解水導引通過該離子交換器,以將該 鹼性電解水之pH値調整在5.5~6.5的範圍,藉以製造高 濃度次氯酸滅菌水。 10. 如申請專利範圍第9項之製造方法,其中電解含氯電解 質溶液以製備鹼性電解水之步驟係持續直到該鹼性電解 ^ 水中自由氯達一預定濃度爲止。 11. 如申請專利範圍第9或10項之製造方法,其中該含氯的 電解質包含鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽 類。 12. 如申請專利範圍第9或10項之製造方法,其中在該含氯 電解質溶液之溶質爲氯化鈉的情況下,該含氯電解質溶 液包括過飽和、飽和或未飽和食鹽水、海水、滷水或生 理食鹽水。 φ 13. —種高濃度次氯酸滅菌水之製造方法,其包含下列步驟: 以無隔膜電解法電解含氯電解質溶液以製備鹼性電解 水;及 以隔膜電解法於陽極側電解槽,電解該鹼性電解水一 預設時間,以將該鹼性電解水之pH値調整在5.5〜6.5的 範圍,藉以製造高濃度次氯酸滅菌水。 I4. 一種高濃度次氯酸滅菌水之製造方法,其包含下列步驟: 以無隔膜電解法電解含氯電解質溶液以製備鹼性電解 水;及 -12- [S] 201102457 以離子交換法將該鹼性電解水之PH値調整在5·5〜6_5 的範圍,藉以製造髙濃度次氯酸滅菌水。 15. —種高濃度次氯酸滅菌水之製造裝置,其包含一無隔膜 電解裝置及一隔膜電解裝置,其中 該無隔膜電解裝置係配置有陽極及陰極’用於電解含 氯電解質溶液,以製備鹼性電解水’ 該隔膜電解裝置包含以隔膜分隔的陽極側電解槽及陰 極側電解槽,於該陽極側電解槽中配置有陽極,於該陰 ^ 極側電解槽中配置有陰極, 該無隔膜電解裝置及隔膜電解裝置係配置成該無隔膜 電解裝置製備的鹼性電解水可導引至該隔膜電解裝置之 陽極側電解槽,藉由該隔膜電解裝置電解該陽極側電解 槽中之該鹼性電解水,而將該鹼性電解水之pH値調整在 5.5〜6.5的範圔,藉以製造高濃度次氯酸滅菌水。 16. 如申請專利範圍第15項之製造裝置,其中該含氯的電解 質包含鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽類。 φ 17.如申請專利範圍第15項之製造方法,其中在該含氯電解 質溶液之溶質爲氯化鈉的情況下,該含氯電解質溶液包 括過飽和、飽和或未飽和食鹽水、海水、滷水或生理食 鹽水。 18. —種高濃度次氯酸滅菌水之製造裝置,其包含三極式有 隔膜電解裝置及切換裝置,其中 該三極式有隔膜電解裝置包含以隔膜分隔的第1電解 槽及第2電解槽,該第1電解槽係配置有第1電極及第2 電極,該第2電解槽係配置有第3電極,該第1電極係 [S3 -13- 201102457 可恆常地或可控制地作用成陽極,而該第2及3電極之 每一者可藉由該切換裝置切換地作用成陽極或陰極; 當藉由該切換裝置使該第2電極作用成陰極時,配合 作用成陽極的第1電極,該第1電解槽係作用成無隔膜 電解裝置,用於電解該第1電解槽中含氯電解質溶液以 製備鹼性電解水: 當藉由該切換裝置使該第3電極作用成陰極時,配合 作用成陽極的第1電極,電解該第2電解槽中的該鹼性 φ 電解水,而將該鹼性電解水之pH値調整在5.5〜6.5的範 圍,藉以製造高濃度次氯酸滅菌水。 19. 如申請專利範圍第18項之製造裝置,其中該含氯的電解 質包含鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽類。 20. 如申請專利範圍第18項之製造裝置,其中在該含氯電解 質溶液之溶質爲氯化鈉的情況下,該含氯電解質溶液包 括過飽和、飽和或未飽和食鹽水、海水、滷水或生理食 鹽水。 φ 21. —種高濃度次氯酸滅菌水之製造裝置,其包含四極式有 隔膜電解裝置及切換裝置,其中 該4極式有隔膜電解裝置包含以隔膜分隔的第1電解 槽及第2電解槽,該第1電解槽係配置有第1電極及第2 電極,該第2電解槽係配置有第3電極及第4電極,該 第1、2、3及4電極之每一者可藉由該切換裝置切換成 陽極或陰極; 當藉由該切換裝置使該第1電極及該第2電極之一者 作用成陽極並使該第1電極及該第2電極之另一者作用 [S1 -14- 201102457 成陰極時,該第1電解槽係作用成無隔膜電解裝置,用 於電解該第1電解槽中含氯電解質溶液以製備鹼性電解 水; 當藉由該切換裝置使該第3電極及/或第4電極作用成 陰極且使該第1電極及/或該第2電極作用成陽極,電解 該第2電解槽中的該鹼性電解水,而將該鹼性電解水之 pH値調整在5_5〜6.5的範圍,藉以製造高濃度次氯酸滅 菌水。 22. 如申請專利範圍第21項之製造裝置,其中該含氯的電解 質包含鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽類。 23. 如申請專利範圍第21項之製造裝置,其中在該含氯電解 質溶液之溶質爲氯化鈉的情況下,該含氯電解質溶液包 括過飽和、飽和或未飽和食鹽水、海水、滷水或生理食 鹽水。 24. —種高濃度次氯酸滅菌水之製造裝置’其包含一個以上 的無隔膜電解裝置及一離子交換器,其中 該無隔膜電解裝置係配置有陽極及陰極’用於電解含 氯電解質溶液,以製備鹼性電解水’ 該離子交換器係收容有陽離子交換樹脂’藉由將該驗 性電解水導引通過該該離子交換器’而將該驗性電解水 之pH値調整在5.5 ~6.5的範圍,藉以製造高濃度次氯酸 滅菌水。 2 5.如申請專利範圍第24項之製造裝置’其中該含氯的電解 質包含鹼金屬氯化物、鹼土金屬氯化物或含氯的鹽類° 26.如申請專利範圍第24項之製造裝置’其中在該含氯18解 f S3 -15- 201102457 質溶液之溶質爲氯化鈉的情況下,該含氯電解質溶液包 V 括過飽和、飽和或未飽和食鹽水、海水、滷水或生理食 鹽水。201102457 VII. Patent application scope: 1. A method for manufacturing high concentration hypochlorite sterilized water, which comprises the following steps: 9 providing a diaphragmless electrolysis device, wherein an anode and a cathode are disposed; and a diaphragm electrolysis device comprising An anode-side electrolytic cell and a cathode-side electrolytic cell, which are separated by a separator, are disposed in the anode-side electrolytic cell, and an anode is disposed in the cathode-side electrolytic cell, and a conductive electrolyte solution is accommodated in the electrolytic cell: Electrolyzing a chlorine-containing electrolyte solution to prepare alkaline electrolyzed water; guiding the alkaline electrolyzed water to an anode-side electrolysis cell of the diaphragm electrolyzer; and electrolyzing the alkaline electrolyzed water by the diaphragm electrolysis device for a predetermined time The pH of the alkaline electrolyzed water is adjusted in the range of 5. 5 to 6.5, thereby producing a high concentration of hypochloric acid sterilized water. 2. The manufacturing method according to claim 1, wherein the step of electrolyzing the chlorine-containing electrolyte solution to prepare the alkaline electrolyzed water is continued until the free chlorine in the alkaline electrolysis φ water reaches a predetermined concentration. 3. The manufacturing method of claim 1 or 2, wherein the chlorine-containing electrolyte comprises an alkali metal chloride, an alkaline earth metal chloride or a chlorine-containing salt. 4) The manufacturing method according to claim 1 or 2, wherein, in the case where the solute of the chlorine-containing electrolyte solution is sodium chloride, the chlorine-containing electrolyte solution comprises supersaturated, saturated or unsaturated brine, seawater, brine Or physiological saline. 5. A method for producing high-concentration hypochlorite sterilized water, comprising the following steps: [S] -10- 201102457 A multi-pole diaphragm electrolysis device comprising a first electrolytic cell separated by a diaphragm and a second electrolysis The first electrolytic cell is provided with a first electrode and a second electrode, and the second electrolytic cell is provided with at least a third electrode and accommodates a conductive electrolyte solution. The first electrode is constantly or controllably Acting as an anode ' and the 2 and 3 electrodes can be switched to act as an anode or a cathode; and preparing a chlorine-containing electrolyte solution in the first electrolytic cell by a first electrode acting as an anode and a second electrode acting as a cathode The alkaline electrolysis electrolyzes the alkaline electrolyzed water in the first electrolysis cell by a first electrode acting as an anode and a third electrode acting as a cathode for a predetermined time to adjust the pH of the alkaline electrolyzed water to A range of 5.5 to 6.5 to produce a high concentration of hypochloric acid sterilized water. 6. The manufacturing method of claim 5, wherein the step of electrolyzing the chlorine-containing electrolyte solution in the first electrolytic cell to prepare alkaline electrolyzed water is continued until the free chlorine in the alkaline electrolyzed water reaches a predetermined concentration; Φ 7· The manufacturing method of claim 5, wherein the chlorine-containing electrolyte comprises an alkali metal chloride, an alkaline earth metal chloride or a chlorine-containing salt. 8. The scope of claim 5 or 6 The manufacturing method, wherein, in the case where the solute of the chlorine-containing electrolyte solution is sodium chloride, the chlorine-containing electrolyte solution includes supersaturated, saturated or unsaturated saline, sea water, brine or physiological saline. A method for producing high-concentration hypochlorite sterilized water, comprising the steps of: providing a diaphragmless electrolysis device having an anode and a cathode disposed therein; [S3 -11 - 201102457 providing an ion exchanger accommodating a cation Exchanging resin; electrolyzing a chlorine-containing electrolyte solution by the diaphragmless electrolysis device to prepare alkaline electrolyzed water; adjusting the pH of the alkaline electrolyzed water by adjusting the alkaline electrolyzed water through the ion exchanger A range of 5.5 to 6.5 to produce a high concentration of hypochloric acid sterilized water. 10. The manufacturing method according to claim 9, wherein the step of electrolyzing the chlorine-containing electrolyte solution to prepare the alkaline electrolyzed water is continued until the free chlorine in the alkaline electrolysis water reaches a predetermined concentration. 11. The method of manufacture of claim 9 or 10, wherein the chlorine-containing electrolyte comprises an alkali metal chloride, an alkaline earth metal chloride or a chlorine-containing salt. 12. The manufacturing method according to claim 9 or 10, wherein, in the case where the solute of the chlorine-containing electrolyte solution is sodium chloride, the chlorine-containing electrolyte solution comprises supersaturated, saturated or unsaturated brine, seawater, brine Or physiological saline. Φ 13. A method for producing high-concentration hypochlorite sterilized water, comprising the steps of: electrolyzing a chlorine-containing electrolyte solution by a diaphragm-free electrolysis method to prepare alkaline electrolyzed water; and electrolyzing the anode on the anode side by electrolysis The alkaline electrolyzed water is adjusted to a pH of 5.5 to 6.5 for a predetermined period of time to produce a high concentration of hypochloric acid sterilized water. I4. A method for producing high-concentration hypochlorite sterilized water, comprising the steps of: electrolyzing a chlorine-containing electrolyte solution by a diaphragm-free electrolysis method to prepare alkaline electrolyzed water; and -12- [S] 201102457 by ion exchange method The pH of the alkaline electrolyzed water is adjusted in the range of 5·5 to 6_5 to produce a sputum concentration of hypochlorite sterilized water. 15. A high concentration hypochlorite sterilized water manufacturing apparatus comprising a diaphragmless electrolysis device and a diaphragm electrolysis device, wherein the diaphragmless electrolysis device is provided with an anode and a cathode for electrolyzing a chlorine-containing electrolyte solution, The alkaline electrolysis water is prepared. The diaphragm electrolysis device includes an anode side electrolysis cell and a cathode side electrolysis cell separated by a separator. An anode is disposed in the anode side electrolysis cell, and a cathode is disposed in the cathode side electrolysis cell. The diaphragmless electrolysis device and the diaphragm electrolysis device are configured such that the alkaline electrolyzed water prepared by the diaphragmless electrolysis device can be guided to the anode side electrolysis cell of the diaphragm electrolysis device, and the anode electrolysis cell is electrolyzed by the diaphragm electrolysis device. The alkaline electrolyzed water is adjusted to a pH of 5.5 to 6.5 by the pH of the alkaline electrolyzed water to produce a high concentration of hypochloric acid sterilized water. 16. The manufacturing apparatus of claim 15, wherein the chlorine-containing electrolyte comprises an alkali metal chloride, an alkaline earth metal chloride or a chlorine-containing salt. Φ 17. The manufacturing method of claim 15, wherein in the case where the solute of the chlorine-containing electrolyte solution is sodium chloride, the chlorine-containing electrolyte solution comprises supersaturated, saturated or unsaturated brine, seawater, brine or Physiological saline solution. 18. A manufacturing apparatus for high-concentration hypochlorite sterilized water, comprising a three-electrode diaphragm electrolysis apparatus including a first electrolytic cell separated by a diaphragm and a second electrolytic device, and a switching device a first electrode and a second electrode are disposed in the first electrolytic cell, and a third electrode is disposed in the second electrolytic cell, and the first electrode system [S3 - 13 - 201102457 can function constantly or controllably Forming an anode, and each of the second and third electrodes can be switched to function as an anode or a cathode by the switching device; when the second electrode acts as a cathode by the switching device, the anode is combined a first electrode, which functions as a diaphragmless electrolysis device for electrolyzing a chlorine-containing electrolyte solution in the first electrolytic cell to prepare alkaline electrolyzed water: when the third electrode acts as a cathode by the switching device At the same time, the first electrode of the anode is combined to electrolyze the alkaline φ electrolyzed water in the second electrolytic cell, and the pH of the alkaline electrolyzed water is adjusted to a range of 5.5 to 6.5, thereby producing a high concentration of hypochlorite. Acid sterilized water. 19. The manufacturing apparatus of claim 18, wherein the chlorine-containing electrolyte comprises an alkali metal chloride, an alkaline earth metal chloride or a chlorine-containing salt. 20. The manufacturing apparatus of claim 18, wherein, in the case where the solute of the chlorine-containing electrolyte solution is sodium chloride, the chlorine-containing electrolyte solution comprises supersaturated, saturated or unsaturated saline, seawater, brine or physiological Saline solution. Φ 21. A manufacturing apparatus for high-concentration hypochlorite sterilized water, comprising a four-pole diaphragm electrolysis device including a first electrolytic cell separated by a diaphragm and a second electrolytic device, and a switching device In the first electrolytic cell, a first electrode and a second electrode are disposed, and the second electrode and the fourth electrode are disposed in the second electrolytic cell, and each of the first, second, third and fourth electrodes can be borrowed Switching to an anode or a cathode by the switching device; wherein one of the first electrode and the second electrode acts as an anode by the switching device, and the other of the first electrode and the second electrode acts [S1 -14- 201102457 When the cathode is formed, the first electrolytic cell acts as a diaphragmless electrolysis device for electrolyzing the chlorine-containing electrolyte solution in the first electrolytic cell to prepare alkaline electrolyzed water; The three electrodes and/or the fourth electrode act as a cathode, and the first electrode and/or the second electrode act as an anode, and the alkaline electrolyzed water in the second electrolytic cell is electrolyzed, and the alkaline electrolyzed water is pH値 is adjusted in the range of 5_5~6.5 to produce high concentration of hypochlorous acid. Water. 22. The manufacturing apparatus of claim 21, wherein the chlorine-containing electrolyte comprises an alkali metal chloride, an alkaline earth metal chloride or a chlorine-containing salt. 23. The manufacturing apparatus according to claim 21, wherein in the case where the solute of the chlorine-containing electrolyte solution is sodium chloride, the chlorine-containing electrolyte solution comprises supersaturated, saturated or unsaturated saline, seawater, brine or physiological Saline solution. 24. A high concentration hypochlorite sterilized water manufacturing apparatus comprising: more than one diaphragmless electrolysis apparatus and an ion exchanger, wherein the diaphragmless electrolysis apparatus is provided with an anode and a cathode for electrolyzing a chlorine-containing electrolyte solution In order to prepare alkaline electrolyzed water, the ion exchanger contains a cation exchange resin, and the pH of the electrolyzed electrolyzed water is adjusted to 5.5 by directing the electrophoretic electrolyzed water through the ion exchanger. Scope of 6.5, in order to produce high concentration of hypochloric acid sterilized water. 2 5. The manufacturing apparatus of claim 24, wherein the chlorine-containing electrolyte comprises an alkali metal chloride, an alkaline earth metal chloride or a chlorine-containing salt. 26. A manufacturing apparatus according to claim 24 of the patent application scope. Wherein the solute of the chlorine-containing 18 solution f S3 -15- 201102457 is sodium chloride, the chlorine-containing electrolyte solution comprises supersaturated, saturated or unsaturated saline, sea water, brine or physiological saline. -16- [S]-16- [S]
TW98123707A 2009-07-14 2009-07-14 Method and apparatus for producing high concentration hypochlorochloride sterilized water TWI427189B (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI506166B (en) * 2011-04-08 2015-11-01 Omega Co Ltd Drainage treatment method
CN111763952A (en) * 2020-07-01 2020-10-13 辽宁黄花沟田园综合体开发有限公司 Desalination method and device for preparing ultra-high-purity hypochlorous acid aqueous solution by using salt as raw material

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CN100451175C (en) * 2005-02-02 2009-01-14 华东理工大学 Preparation of hypochlorous and disinfectant liquid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI506166B (en) * 2011-04-08 2015-11-01 Omega Co Ltd Drainage treatment method
CN111763952A (en) * 2020-07-01 2020-10-13 辽宁黄花沟田园综合体开发有限公司 Desalination method and device for preparing ultra-high-purity hypochlorous acid aqueous solution by using salt as raw material

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