TWI605020B - Continuous waste water treatment device and treatment method - Google Patents

Continuous waste water treatment device and treatment method Download PDF

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TWI605020B
TWI605020B TW105137715A TW105137715A TWI605020B TW I605020 B TWI605020 B TW I605020B TW 105137715 A TW105137715 A TW 105137715A TW 105137715 A TW105137715 A TW 105137715A TW I605020 B TWI605020 B TW I605020B
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Taiwan
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tank
sterilization
partition
wastewater
sterilization tank
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TW105137715A
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TW201819312A (en
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Shuo-Jen Lee
Qi-Wang Li
Sheng-Ming Zhuang
Huan-Zhi Peng
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Shuo-Jen Lee
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Publication of TW201819312A publication Critical patent/TW201819312A/en

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Description

連續式之廢水的處理裝置及處理方法Continuous wastewater treatment device and treatment method

本發明係有關一種連續式之廢水的處理裝置及處理方法,尤指一種兼具可連續式處理相當方便、氣泡供應部之液體擾動效果提高,同時連續處理並進行保養維修相當方便之連續式之廢水的處理裝置及處理方法。The invention relates to a continuous type of waste water treatment device and a treatment method thereof, in particular to a continuous type which has the advantages that the continuous treatment is convenient, the liquid disturbance effect of the bubble supply part is improved, and the continuous treatment and the maintenance and repair are quite convenient. Wastewater treatment equipment and treatment methods.

現今廢水來源種類很多,可能包括工業廢水、醫療單位廢水(例如洗腎病房或是手術室之廢水,就可能以血水、體內液體為主)、各式場合之清洗廢水。廢水必須先經過殺菌處理(最好再經過濾及相關之除污處理),才能再排放至一般之公共排水系統。 目前已有許多殺菌裝置是利用電解水技術來達成,當利用直流電源之兩極來連接一對電極進行電解食鹽水時,陽極會生成氯氣,而氯氣若未即時導出,則會溶解水,產生次氯酸分子(HClO)和解離狀態的鹽酸。由於鈉離子無法和水分子競爭電子,所以陰極和電解稀鹽水時的情形相同,會生成氫氣與解離狀態的氫氧化鈉。 當次氯酸在與細菌接觸時,會產生氧化作用使微生物的蛋白質變質,有效消滅細菌、真菌及病毒。不但可以作用於細胞壁、病毒外殼,更因次氯酸分子小且不帶電荷,還可滲透入菌(或病毒)體內,與菌(或病毒)體蛋白、核酸等有機高分子發生氧化反應,從而殺死病原微生物(例如包含:沙門氏菌、金黃色葡萄球菌、彎曲弧菌、李氏桿菌及大腸桿菌等),且使用後的次氯酸(HClO)也會還原成對人體無害的水。 然而,傳統之廢水在進行殺菌處理時(例如在處理醫療廢水時),均為一箱一箱(或一桶一桶)之非連續式處理,移動及暫存之處理均十分麻煩。 此外,廢水在進行傳統技術之殺菌處理時會產生膠狀物,膠狀物會影響流動性或黏附在電極上,所產生之沉澱物也不易清理。 因此,有必要研發新技術,以解決現有缺點。There are many types of wastewater sources today, which may include industrial wastewater, medical unit wastewater (such as dialysis wards or operating room wastewater, which may be mainly blood and water), and cleaning wastewater for various occasions. The wastewater must be sterilized (preferably filtered and associated with decontamination) before it can be discharged to the general public drainage system. At present, many sterilizing devices are realized by using electrolyzed water technology. When two poles of a direct current power source are used to connect a pair of electrodes for electrolyzing brine, the anode generates chlorine gas, and if the chlorine gas is not immediately exported, the water is dissolved and generated. Chlorinated acid molecules (HClO) and hydrochloric acid in a dissociated state. Since sodium ions cannot compete with water molecules for electrons, the cathode is the same as in the case of electrolytic dilute brine, and hydrogen gas and dissociated sodium hydroxide are generated. When hypochlorous acid is in contact with bacteria, it will produce oxidation to degrade the protein of the microorganism, effectively destroying bacteria, fungi and viruses. It can not only act on the cell wall, virus shell, but also because hypochlorous acid molecules are small and uncharged, and can also penetrate into bacteria (or viruses), and oxidize with organic polymers such as bacteria (or virus) body proteins and nucleic acids. Thereby killing pathogenic microorganisms (for example, including: Salmonella, Staphylococcus aureus, Vibrio cholerae, Listeria, Escherichia coli, etc.), and the hypochlorous acid (HClO) after use is also reduced to water which is harmless to the human body. However, when the conventional wastewater is sterilized (for example, when treating medical wastewater), it is a non-continuous treatment of one case, one case (or one barrel and one barrel), and the handling of movement and temporary storage is very troublesome. In addition, the waste water will produce a gel when subjected to sterilization by conventional techniques, and the gel will affect the fluidity or adhere to the electrode, and the precipitate produced is not easy to clean. Therefore, it is necessary to develop new technologies to solve the existing shortcomings.

本發明之目的,在於提供一種連續式之廢水的處理裝置及處理方法,其兼具可連續式處理相當方便、氣泡供應部之液體擾動效果提高,可同時連續處理並進行保養維修相當方便等優點。特別是,本發明所欲解決之問題係在於傳統廢水之殺菌處理均為一箱一箱(或一桶一桶)之非連續式處理,移動及暫存之處理均十分麻煩等問題。 解決上述問題之技術手段係提供一種連續式之廢水的處理裝置及處理方法,該處理裝置係設至少一個,該每一處理裝置包括: 一控制部; 一連續處理部,係連結該控制部,並具有依序相連通之一進水容納槽、一電解殺菌槽、一沉澱槽及一出水容納槽;其中:該進水容納槽係供一廢水流入;該出水容納槽係供該廢水流出; 一電極殺菌部,係懸設於該電解殺菌槽內,並包括:一正電極板、一負電極板、複數個介於其間且彼此不接觸之電感應極板;該控制部係用以對該正電極板供應一正電,且該控制部係用以對該負電極板供應一負電; 一氣泡供應部,係設於該電解殺菌槽內,且位於該電極殺菌部下方,該氣泡供應部係設一供氣裝置及至少一排氣管;該排氣管具有至少一排氣口;該控制部係連接該供氣裝置,用以控制該供氣裝置對該排氣管供入一空氣,該空氣經該至少一排氣口供入該電解殺菌槽內而形成複數個氣泡; 一擾流部,係呈板狀結構,其一端係懸設於沉澱槽其鄰近該出水容納槽的該端,且另端係傾斜向下而朝該電解殺菌槽的方向延伸; 藉此,該廢水於流入再流出該連續處理部的過程中,且該電極殺菌部被供電時,係可與該廢水反應而產生次氯酸水,進而對該廢水產生殺菌作用,同時,該排氣口產生之複數個氣泡,係從該電解殺菌槽底部向上移動,移動過程可帶走該電解殺菌槽內相關結構上之污物,且該擾流部係使該廢水於該沉澱槽內先呈反向渦流捲動後,方流入該出水容納槽,用以提高沉澱效果,達成連續式之廢水的處理裝置。 關於本發明之處理方法,係包括下列步驟: 一、準備步驟; 二、連續進水步驟; 三、殺菌步驟; 四、氣泡擾動除污步驟; 五、擾流除污步驟; 六、完成步驟。 本發明之上述目的與優點,不難從下述所選用實施例之詳細說明與附圖中,獲得深入瞭解。 茲以下列實施例並配合圖式詳細說明本發明於後:The object of the present invention is to provide a continuous waste water treatment device and a treatment method thereof, which are convenient for continuous treatment, liquid disturbance effect of the bubble supply portion, and can be continuously processed and maintained at a convenient time. . In particular, the problem to be solved by the present invention is that the sterilization treatment of the conventional wastewater is a non-continuous treatment of one case, one case (or one barrel and one barrel), and the handling of the movement and the temporary storage are very troublesome. The technical means for solving the above problems is to provide a continuous waste water treatment device and a treatment method. The treatment device is provided with at least one. Each of the treatment devices includes: a control unit; and a continuous processing unit that is coupled to the control unit. And having a water inlet tank, an electrolytic sterilization tank, a sedimentation tank and a water receiving tank; wherein: the water inlet tank is for a wastewater to flow; the water receiving tank is for discharging the wastewater; An electrode sterilization unit is suspended in the electrolysis sterilization tank and includes: a positive electrode plate, a negative electrode plate, and a plurality of electric induction plates interposed therebetween and not in contact with each other; the control portion is used for The positive electrode plate is supplied with a positive power, and the control portion is configured to supply a negative power to the negative electrode plate; a bubble supply portion is disposed in the electrolytic sterilization tank and located below the electrode sterilization portion, the bubble supply The air supply device and the at least one exhaust pipe; the exhaust pipe has at least one exhaust port; the control portion is connected to the air supply device for controlling the air supply device to supply the exhaust pipe air, The air is supplied into the electrolytic sterilization tank through the at least one exhaust port to form a plurality of air bubbles; a spoiler portion is a plate-like structure, and one end thereof is suspended from the sedimentation tank adjacent to the end of the water discharge receiving tank. And the other end is inclined downward to extend in the direction of the electrolysis sterilization tank; thereby, the wastewater can react with the wastewater when flowing and flowing out of the continuous treatment portion, and the electrode sterilization portion is powered Producing hypochlorous acid water to further sterilize the wastewater, and at the same time, a plurality of bubbles generated by the exhaust port move upward from the bottom of the electrolysis sterilization tank, and the moving process can take away the relevant structure in the electrolysis sterilization tank. The sewage, and the spoiler portion causes the waste water to roll in the reverse vortex first in the sedimentation tank, and then flows into the outlet water receiving tank to improve the sedimentation effect, thereby achieving a continuous wastewater treatment device. Regarding the treatment method of the present invention, the following steps are included: 1. Preparation step; 2. Continuous water inflow step; 3. Sterilization step; 4. Bubble disturbing and decontaminating step; 5. Disturbing and decontaminating step; The above objects and advantages of the present invention will be readily understood from the following detailed description of the preferred embodiments illustrated herein. The invention will be described in detail in the following examples in conjunction with the drawings:

參閱第1、第2、第3及第4圖,本發明係為一連續式之廢水的處理裝置及處理方法,該處理裝置係設至少一個,該每一處理裝置可包括一控制部10、一連續處理部20、一電極殺菌部30、一氣泡供應部40及一擾流部50;其中: 關於該控制部10,係電性連結該電極殺菌部30及該氣泡供應部40,用以控制其動作。 關於該連續處理部20,係連結該控制部10,並具有依序相連通之一進水容納槽21、一電解殺菌槽22、一沉澱槽23及一出水容納槽24;其中,該進水容納槽21係供一廢水91流入;該出水容納槽24係供該廢水91流出。 關於該電極殺菌部30,係懸設於該電解殺菌槽22內,並包括一正電極板31、一負電極板32、複數個介於其間且彼此不接觸之電感應極板33(如第9圖所示);該控制部10用以對該正電極板31供應一正電11,且該控制部10係用以對該負電極板32供應一負電12。 關於該氣泡供應部40(如第5A、第5B、第6、第7及第8圖所示),係設於該電解殺菌槽22內,且位於該電極殺菌部30下方,該氣泡供應部40係設一供氣裝置41及至少一排氣管42;該排氣管42具有至少一排氣口421;該控制部10係連接該供氣裝置41,用以控制該供氣裝置41對該排氣管42供入一空氣92,該空氣92經該至少一排氣口421供入該電解殺菌槽22內,用以於該廢水91內形成複數個氣泡92A。 關於該擾流部50,係呈板狀結構,其一端懸設於沉澱槽23其鄰近該出水容納槽24的該端,且另端朝該電解殺菌槽22的方向呈傾斜向下延伸。 藉此,該廢水91於流入再流出該連續處理部20的過程中,且該電極殺菌部30被供電時,係可與該廢水91反應而產生次氯酸水,進而對該廢水91產生殺菌作用,同時,該排氣口421產生之複數個氣泡92A,係從該電解殺菌槽22底部向上移動,移動過程可帶走該電解殺菌槽22內相關結構上之污物(包括該廢水91殺菌過程產生的污物、該各極板上之反應物及黏著物),且該擾流部50係使該廢水91於該沉澱槽23內先呈反向渦流(如第3圖所示)捲動後,方流入該出水容納槽24,用以提高沉澱效果,達成連續式之廢水的處理裝置。 實務上,該電解殺菌槽22可再包括:一第一隔板221、一第二隔板222、一第三隔板223及一第四隔板224,其中,該第一隔板221及該第二隔板222係分別立設於該進水容納槽21內,而隔離出該電解殺菌槽22,該第一隔板221具有一第一高度H1,該第二隔板221具有一第二高度H2,其係低於該第一高度H1;該第三隔板223係立設於該第一隔板221與該第二隔板222之間,而隔離出一第一殺菌槽22A;該第四隔板224係懸設於該第一隔板221及該第三隔板223之間,而隔離出一第二殺菌槽22B及一第三殺菌槽22C,其間具有一底部通口225。藉該第一殺菌槽22A、該第二殺菌槽22B、該底部通口225及該第三殺菌槽22C,係可延長該廢水91於該電解殺菌槽22內被殺菌處理的時間。 更詳細的講,該廢水91流入再流出該電解殺菌槽22之路徑:從該第三殺菌槽22C頂部(槽口)流到該第三殺菌槽22C底部(槽底)→從該第三殺菌槽22C底部(槽底)流向該底部通口225→從該底部通口225流向該第二殺菌槽22B底部(槽底)→從該第二殺菌槽22B底部(槽底)流向該第二殺菌槽22B頂部(槽口)→前述路徑概呈S型而可加長流動殺菌的距離→從該第二殺菌槽22B頂部(槽口)流向該第一殺菌槽22A頂部(槽口)→最後流入該沉澱槽23。 該出水容納槽24係包括一主出水口241及一副出水口242,皆係用以供出殺菌處理後的該廢水91。 該排氣管42可為複數支,且分別並列於該進水容納槽21、該第一殺菌槽22A、該第二殺菌槽22B、該第三殺菌槽22C、該沉澱槽23及該出水容納槽24內(如第3圖所示)。 該排氣口421可為孔結構(如第5A圖所示)、長條孔結構(如第5B圖所示)其中至少一者。 該排氣口421設於該排氣管42上,可為單排結構(如第6圖所示)、雙排結構其中一者,並當為雙排結構(參閱第7圖),該兩排排氣口421之間,可具有一工作角度θ(例如介於5度至15度之間)。 參閱第10圖(主要為數量示意,大部分元件予以省略未示,合先陳明),更進一步來講,該處理裝置可設置複數(例如設置3個)個,且呈並聯,藉此可選擇: [a].3個同時連續處理廢水91。 [b].至少1個進行保養維修,至少1個保持連續處理廢水91。 亦即,可24小時連續處理廢水91,還可兼顧保養維修。 本案應用於醫療單位之廢水處理,可解決一箱一箱(或一桶一桶)之非連續式處理,所造成之移動及暫存之處理均十分麻煩等問題。 參閱第11圖,關於本發明之處理方法部分,於開始後係可包括下列步驟: 一、準備步驟81:預先設置至少一個處理裝置,該每處理裝置係包括一控制部10、一連續處理部20、一電極殺菌部30、一氣泡供應部40及一擾流部50;其中: 關於該控制部10,係電性連結該電極殺菌部30及該氣泡供應部40,用以控制其動作。 關於該連續處理部20,係連結該控制部10,並具有依序相連通之一進水容納槽21、一電解殺菌槽22、一沉澱槽23及一出水容納槽24;其中,該進水容納槽21係供一廢水91流入;該出水容納槽24係供該廢水91流出。 關於該電極殺菌部30,係懸設於該電解殺菌槽22內,並包括一正電極板31、一負電極板32、複數個介於其間且彼此不接觸之電感應極板33(如第10圖所示)。 關於該氣泡供應部40(如第5A、第5B、第6及第7圖所示),係設於該電解殺菌槽22內,且位於該電極殺菌部30下方,該氣泡供應部40設有一供氣裝置41及至少一排氣管42;該排氣管42具有至少一排氣口421;該控制部10係連接該供氣裝置41。 關於該擾流部50,係呈板狀結構,其一端係懸設於沉澱槽23其鄰近該出水容納槽24的該端,且另端係傾斜向下而朝該電解殺菌槽22的方向延伸。 二、連續進水步驟82:將該廢水91連續供入該連續處理部20。 三、殺菌步驟83:透過該控制部10對該正電極板31供應一正電11,且透過該控制部10對該負電極板32供應一負電12,則該廢水91在流過該電極殺菌部30的過程中,係可與該電極殺菌部30反應而生成次氯酸水,進而對該廢水91產生殺菌作用。 四、氣泡擾動除污步驟84:透過該控制部10控制該供氣裝置41對該排氣管42供入一空氣92,該空氣92經該至少一排氣口421供入該電解殺菌槽22內,而形成從該電解殺菌槽22底部向上移動的複數個氣泡92A,該每一氣泡92A於移動過程,除可擾動(增加停留而被殺菌的時間)該廢水91外,並可帶走該電解殺菌槽22內相關結構上之污物(包括該廢水91殺菌過程產生的污物、該各極板上之反應物及黏著物)。 五、擾流除污步驟85:該廢水91從該電解殺菌槽22流入該沉澱槽23後,該擾流部50係使該廢水91於該沉澱槽23內先呈反向渦流捲動後,方流入該出水容納槽24,而不直接順向流入該出水容納槽24,可用以提高沉澱效果。 六、完成步驟86:該廢水91從該出水容納槽24供出後,可供回收再利用。 其中,該電解殺菌槽22可再包括:一第一隔板221、一第二隔板222、一第三隔板223及一第四隔板224,其中,該第一隔板221及該第二隔板222係分別立設於該進水容納槽21內,而隔離出該電解殺菌槽22,該第一隔板221具有一第一高度H1,該第二隔板221具有一第二高度H2,其係低於該第一高度H1;該第三隔板223係立設於該第一隔板221與該第二隔板222之間,而隔離出一第一殺菌槽22A;該第四隔板224係懸設於該第一隔板221及該第三隔板223之間,而隔離出一第二殺菌槽22B及一第三殺菌槽22C,其間具有一底部通口225。藉該第一殺菌槽22A、該第二殺菌槽22B、該底部通口225及該第三殺菌槽22C,係可延長該廢水91於該電解殺菌槽22內被殺菌處理的時間。 該出水容納槽24係包括一主出水口241及一副出水口242,皆係用以供出殺菌處理後的該廢水91。 該排氣管42可為複數支,且分別並列於該進水容納槽21、該第一殺菌槽22A、該第二殺菌槽22B、該第三殺菌槽22C、該沉澱槽23及該出水容納槽24內(如第3圖所示)。 該排氣口421可為孔結構(如第5A圖所示)、長條孔結構(如第5B圖所示)其中至少一者。 該排氣口421設於該排氣管42上,可為單排結構(如第6圖所示)、雙排結構其中一者,並當為雙排結構(參閱第7圖),該兩排排氣口421之間,可具有一工作角度θ(例如介於5度至15度之間)。 參閱第10圖(主要為數量示意,大部分元件予以省略未示,合先陳明),更進一步來講,該處理裝置可設置複數(例如設置3個)個,且呈並聯,藉此可選擇: [a].3個同時連續處理廢水91。 [b].至少1個進行保養維修,至少1個保持連續處理廢水91。 亦即,可24小時連續處理廢水91,還可兼顧保養維修。 本案應用於醫療單位之廢水處理,可解決一箱一箱(或一桶一桶)之非連續式處理,所造成之移動及暫存之處理均十分麻煩等問題。 本發明之優點及功效係如下所述: [1] 可連續式處理相當方便。本發明於連續處理部內設置進水容納槽、電解殺菌槽、沉澱槽及出水容納槽,亦即,(醫療單位)廢水可連續供入該進水容納槽,並連續通過該電解殺菌槽及該沉澱槽,即完成殺菌處理而進入該出水容納槽待供出,相當方便。亦即可將傳統儲置成箱或是成桶的廢水全數倒入該連續處理部進行連續式處理,而不用一箱一箱(或一桶一桶)的非連續式處理。故,可連續式處理相當方便。 [2] 氣泡供應部之液體擾動效果提高。由於電極殺菌部之各電極板上,可能黏附一些反應物或廢水中之雜質,當有氣泡不斷由各電極板底下往上飄移時,這些氣泡不僅可以提高液體擾動效果,一方面降低物體黏附於電極板之機率,另一方面也能將已經黏附於電極板之異物(反應物或廢水中之雜質)帶走。故,氣泡供應部之液體擾動效果提高。 [3] 可同時連續處理並進行保養維修相當方便。本發明之處理裝置可設置複數(例如設置3個)個,且呈並聯,藉此,可選擇3個同時連續處理廢水。或是其中至少1個進行保養維修,其中至少1個保持連續處理廢水。亦即,可24小時連續處理廢水,還可兼顧保養維修。故,可同時連續處理並進行保養維修相當方便。 以上僅是藉由較佳實施例詳細說明本發明,對於該實施例所做的任何簡單修改與變化,皆不脫離本發明之精神與範圍。Referring to the first, second, third and fourth figures, the present invention is a continuous waste water treatment device and a treatment method, the treatment device is provided with at least one, each treatment device may comprise a control portion 10, a continuous processing unit 20, an electrode sterilization unit 30, a bubble supply unit 40, and a spoiler 50. The control unit 10 electrically connects the electrode sterilization unit 30 and the bubble supply unit 40. Control its movements. The continuous processing unit 20 is connected to the control unit 10, and has a water inlet tank 21, an electrolytic sterilization tank 22, a sedimentation tank 23, and a water receiving tank 24 connected in sequence; wherein, the water inlet The accommodating tank 21 is for supplying a wastewater 91, and the effluent accommodating tank 24 is for discharging the wastewater 91. The electrode sterilization unit 30 is suspended in the electrolytic sterilization tank 22 and includes a positive electrode plate 31, a negative electrode plate 32, and a plurality of electric induction plates 33 interposed therebetween and not in contact with each other (eg, The control unit 10 is configured to supply a positive power 11 to the positive electrode plate 31, and the control portion 10 is configured to supply a negative power 12 to the negative electrode plate 32. The bubble supply unit 40 (shown in FIGS. 5A, 5B, 6, 7, and 8) is disposed in the electrolytic sterilization tank 22 and is located below the electrode sterilization unit 30. The bubble supply unit is provided. 40 is provided with a gas supply device 41 and at least one exhaust pipe 42; the exhaust pipe 42 has at least one exhaust port 421; the control portion 10 is connected to the air supply device 41 for controlling the air supply device 41 The exhaust pipe 42 is supplied with an air 92, and the air 92 is supplied into the electrolytic sterilization tank 22 through the at least one exhaust port 421 for forming a plurality of bubbles 92A in the wastewater 91. The spoiler 50 has a plate-like structure, and one end thereof is suspended from the end of the sedimentation tank 23 adjacent to the water discharge receiving groove 24, and the other end extends obliquely downward toward the electrolysis sterilization tank 22. Thereby, the wastewater 91 is in the process of flowing in and out of the continuous processing unit 20, and when the electrode sterilization unit 30 is powered, it can react with the wastewater 91 to generate hypochlorous acid water, thereby sterilizing the wastewater 91. At the same time, the plurality of bubbles 92A generated by the exhaust port 421 are moved upward from the bottom of the electrolytic sterilization tank 22, and the moving process can take away the dirt on the related structure in the electrolytic sterilization tank 22 (including the wastewater 91 sterilization). The dirt generated by the process, the reactants on the plates and the adherends), and the spoiler 50 causes the wastewater 91 to first vortex in the sedimentation tank 23 (as shown in FIG. 3). After the movement, the water flows into the water discharge tank 24 to improve the sedimentation effect, and a continuous waste water treatment device is achieved. In practice, the electrolytic sterilizing tank 22 can further include: a first partition 221, a second partition 222, a third partition 223 and a fourth partition 224, wherein the first partition 221 and the The second partition plate 222 is respectively disposed in the water inlet receiving groove 21 to isolate the electrolytic sterilization tank 22, the first partition plate 221 has a first height H1, and the second partition plate 221 has a second portion. a height H2, which is lower than the first height H1; the third partition 223 is erected between the first partition 221 and the second partition 222 to isolate a first sterilization tank 22A; The fourth partition 224 is suspended between the first partition 221 and the third partition 223 to isolate a second sterilization tank 22B and a third sterilization tank 22C with a bottom opening 225 therebetween. The first sterilization tank 22A, the second sterilization tank 22B, the bottom opening 225, and the third sterilization tank 22C can extend the time during which the wastewater 91 is sterilized in the electrolytic sterilization tank 22. More specifically, the wastewater 91 flows into the path of the electrolysis sterilization tank 22: from the top (notch) of the third sterilization tank 22C to the bottom of the third sterilization tank 22C (the bottom of the tank) → from the third sterilization The bottom of the groove 22C (the bottom of the groove) flows toward the bottom opening 225 → flows from the bottom opening 225 to the bottom of the second sterilization tank 22B (the bottom of the groove) → flows from the bottom of the second sterilization tank 22B (the bottom of the groove) to the second sterilization The top of the groove 22B (notch) → the above-mentioned path is S-shaped and can lengthen the flow sterilization distance → from the top (notch) of the second sterilization tank 22B to the top (notch) of the first sterilization tank 22A → finally flows into the Precipitation tank 23. The effluent receiving tank 24 includes a main water outlet 241 and a pair of water outlets 242 for supplying the sterilized wastewater 97. The exhaust pipe 42 may be a plurality of branches, and are respectively juxtaposed in the water inlet receiving groove 21, the first sterilization tank 22A, the second sterilization tank 22B, the third sterilization tank 22C, the sedimentation tank 23, and the water discharge. Inside the slot 24 (as shown in Figure 3). The exhaust port 421 can be at least one of a hole structure (as shown in FIG. 5A) and a long hole structure (as shown in FIG. 5B). The exhaust port 421 is disposed on the exhaust pipe 42 and can be a single row structure (as shown in FIG. 6) and a double row structure, and is a double row structure (refer to FIG. 7). Between the exhaust ports 421, there may be a working angle θ (for example, between 5 and 15 degrees). Referring to Figure 10 (mainly for the number, most of the components are omitted, not shown), and further, the processing device can be set to a plurality of (for example, set 3), and in parallel, thereby Choice: [a].3 simultaneous treatment of wastewater 91. [b]. At least one maintenance and repair, at least one of which maintains continuous treatment of wastewater 91. That is, the wastewater 91 can be continuously treated for 24 hours, and maintenance and repair can be achieved. The case is applied to the wastewater treatment of the medical unit, which can solve the discontinuous treatment of one box and one box (or one barrel and one barrel), and the handling of the movement and the temporary storage are very troublesome. Referring to FIG. 11, the processing method portion of the present invention may include the following steps after the start: 1. Preparation step 81: at least one processing device is provided in advance, the processing device includes a control unit 10 and a continuous processing unit. 20. An electrode sterilization unit 30, a bubble supply unit 40, and a spoiler 50. The control unit 10 electrically connects the electrode sterilization unit 30 and the bubble supply unit 40 to control the operation thereof. The continuous processing unit 20 is connected to the control unit 10, and has a water inlet tank 21, an electrolytic sterilization tank 22, a sedimentation tank 23, and a water receiving tank 24 connected in sequence; wherein, the water inlet The accommodating tank 21 is for supplying a wastewater 91, and the effluent accommodating tank 24 is for discharging the wastewater 91. The electrode sterilization unit 30 is suspended in the electrolytic sterilization tank 22 and includes a positive electrode plate 31, a negative electrode plate 32, and a plurality of electric induction plates 33 interposed therebetween and not in contact with each other (eg, Figure 10 shows). The bubble supply unit 40 (shown in FIGS. 5A, 5B, 6 and 7) is disposed in the electrolytic sterilization tank 22 and is located below the electrode sterilization unit 30. The bubble supply unit 40 is provided with a The air supply device 41 and the at least one exhaust pipe 42; the exhaust pipe 42 has at least one exhaust port 421; the control portion 10 is connected to the air supply device 41. The spoiler 50 has a plate-like structure, and one end thereof is suspended from the end of the sedimentation tank 23 adjacent to the water discharge receiving groove 24, and the other end is inclined downward and extends toward the electrolytic sterilization tank 22. . 2. Continuous water inflow step 82: The wastewater 91 is continuously supplied to the continuous treatment unit 20. 3. Sterilization step 83: a positive electric power 11 is supplied to the positive electrode plate 31 through the control unit 10, and a negative electric power 12 is supplied to the negative electrode plate 32 through the control unit 10, and the waste water 91 is sterilized by flowing through the electrode. In the process of the portion 30, it is possible to react with the electrode sterilization unit 30 to generate hypochlorous acid water, thereby generating a bactericidal action on the wastewater 91. 4. Bubble disturbance decontamination step 84: The air supply device 41 is controlled by the control unit 10 to supply an air 92 to the exhaust pipe 42 . The air 92 is supplied to the electrolytic sterilization tank 22 via the at least one exhaust port 421 . And forming a plurality of air bubbles 92A moving upward from the bottom of the electrolytic sterilization tank 22, and each of the air bubbles 92A is in a moving process, except for the waste water 91 which can be disturbed (increased staying and being sterilized), and can take away the The dirt on the relevant structure in the electrolytic sterilization tank 22 (including the dirt generated by the sterilization process of the wastewater 91, the reactants and the adhesive on the respective plates). V. Spoiler Decontamination Step 85: After the wastewater 91 flows from the electrolysis sterilization tank 22 into the sedimentation tank 23, the spoiler 50 causes the wastewater 91 to first scroll in the sedimentation tank 23 by a reverse vortex. The square flows into the outlet water receiving tank 24 without directly flowing into the outlet water receiving tank 24, which can be used to enhance the sedimentation effect. 6. Step 86: After the wastewater 91 is supplied from the water receiving tank 24, it can be recycled and reused. The electrolysis sterilization tank 22 may further include: a first partition 221, a second partition 222, a third partition 223 and a fourth partition 224, wherein the first partition 221 and the first The two partition plates 222 are respectively disposed in the water inlet receiving groove 21 to isolate the electrolytic sterilization tank 22, the first partition plate 221 has a first height H1, and the second partition plate 221 has a second height. H2, which is lower than the first height H1; the third partition 223 is erected between the first partition 221 and the second partition 222, and isolates a first sterilization tank 22A; The four partitions 224 are suspended between the first partition 221 and the third partition 223 to isolate a second sterilization tank 22B and a third sterilization tank 22C with a bottom opening 225 therebetween. The first sterilization tank 22A, the second sterilization tank 22B, the bottom opening 225, and the third sterilization tank 22C can extend the time during which the wastewater 91 is sterilized in the electrolytic sterilization tank 22. The effluent receiving tank 24 includes a main water outlet 241 and a pair of water outlets 242 for supplying the sterilized wastewater 97. The exhaust pipe 42 may be a plurality of branches, and are respectively juxtaposed in the water inlet receiving groove 21, the first sterilization tank 22A, the second sterilization tank 22B, the third sterilization tank 22C, the sedimentation tank 23, and the water discharge. Inside the slot 24 (as shown in Figure 3). The exhaust port 421 can be at least one of a hole structure (as shown in FIG. 5A) and a long hole structure (as shown in FIG. 5B). The exhaust port 421 is disposed on the exhaust pipe 42 and can be a single row structure (as shown in FIG. 6) and a double row structure, and is a double row structure (refer to FIG. 7). Between the exhaust ports 421, there may be a working angle θ (for example, between 5 and 15 degrees). Referring to Figure 10 (mainly for the number, most of the components are omitted, not shown), and further, the processing device can be set to a plurality of (for example, set 3), and in parallel, thereby Choice: [a].3 simultaneous treatment of wastewater 91. [b]. At least one maintenance and repair, at least one of which maintains continuous treatment of wastewater 91. That is, the wastewater 91 can be continuously treated for 24 hours, and maintenance and repair can be achieved. The case is applied to the wastewater treatment of the medical unit, which can solve the discontinuous treatment of one box and one box (or one barrel and one barrel), and the handling of the movement and the temporary storage are very troublesome. The advantages and functions of the present invention are as follows: [1] Continuous processing is quite convenient. The invention provides a water inlet tank, an electrolytic sterilization tank, a sedimentation tank and a water discharge tank in the continuous processing section, that is, (medical unit) wastewater can be continuously supplied into the water inlet tank, and continuously passes through the electrolytic sterilization tank and the The sedimentation tank, that is, the sterilization treatment is completed, and enters the water discharge tank to be supplied, which is quite convenient. It is also possible to pour all of the conventionally stored tanks or barrels of waste water into the continuous processing section for continuous processing without the use of a box of one tank (or one bucket and one bucket) of discontinuous treatment. Therefore, continuous processing is quite convenient. [2] The liquid perturbation effect of the bubble supply unit is improved. Since some electrode materials on the electrode sterilizing part may adhere to some reactants or impurities in the waste water, when bubbles continuously flow from the bottom of each electrode plate, the bubbles not only improve the liquid perturbation effect, but also reduce the adhesion of the object on the one hand. The probability of the electrode plate, on the other hand, can also carry away foreign matter (impurities in the reactants or waste water) that have adhered to the electrode plate. Therefore, the liquid perturbation effect of the bubble supply portion is improved. [3] It is quite convenient to process and carry out maintenance at the same time. The processing apparatus of the present invention can be provided in plural (for example, three), and in parallel, whereby three simultaneous wastewater treatments can be selected. Or at least one of them is maintained, at least one of which maintains continuous treatment of wastewater. That is, the wastewater can be continuously treated for 24 hours, and maintenance and repair can be considered. Therefore, it is quite convenient to continuously process and perform maintenance at the same time. The present invention has been described in detail with reference to the preferred embodiments of the present invention, without departing from the spirit and scope of the invention.

10‧‧‧控制部10‧‧‧Control Department

11‧‧‧正電11‧‧‧正正

12‧‧‧負電12‧‧‧ Negative electricity

20‧‧‧連續處理部20‧‧‧Continuous Processing Department

21‧‧‧進水容納槽21‧‧‧Intake tank

22‧‧‧電解殺菌槽22‧‧‧ Electrolytic sterilization tank

221‧‧‧第一隔板221‧‧‧ first partition

222‧‧‧第二隔板222‧‧‧Second partition

223‧‧‧第三隔板223‧‧‧ third partition

224‧‧‧第四隔板224‧‧‧4th partition

225‧‧‧底部通口225‧‧‧ bottom port

22A‧‧‧第一殺菌槽22A‧‧‧First sterilization tank

22B‧‧‧第二殺菌槽22B‧‧‧Second sterilization tank

22C‧‧‧第三殺菌槽22C‧‧‧The third sterilization tank

23‧‧‧沉澱槽23‧‧‧Sedimentation tank

24‧‧‧出水容納槽24‧‧‧Water receiving tank

241‧‧‧主出水口241‧‧‧Main outlet

242‧‧‧副出水口242‧‧‧ Deputy outlet

30‧‧‧電極殺菌部30‧‧‧Electrode sterilization department

31‧‧‧正電極板31‧‧‧ positive electrode plate

32‧‧‧負電極板32‧‧‧Negative electrode plate

33‧‧‧電感應極板33‧‧‧Electrical induction plates

40‧‧‧氣泡供應部40‧‧‧ Bubble Supply Department

41‧‧‧供氣裝置41‧‧‧ gas supply

42‧‧‧排氣管42‧‧‧Exhaust pipe

421‧‧‧排氣口421‧‧‧Exhaust port

50‧‧‧擾流部50‧‧‧Surveying Department

81‧‧‧準備步驟81‧‧‧Preparation steps

82‧‧‧連續進水步驟82‧‧‧Continuous water intake steps

83‧‧‧殺菌步驟83‧‧‧Sterilization steps

84‧‧‧氣泡擾動除污步驟84‧‧‧ Bubble disturbance decontamination step

85‧‧‧擾流除污步驟85‧‧‧Spoil removal and decontamination steps

86‧‧‧完成步驟86‧‧‧Complete steps

91‧‧‧廢水91‧‧‧ Wastewater

92‧‧‧空氣92‧‧‧ Air

92A‧‧‧氣泡92A‧‧‧ bubble

H1‧‧‧第一高度H1‧‧‧ first height

H2‧‧‧第二高度H2‧‧‧second height

θ‧‧‧工作角度Θ‧‧‧ working angle

第1圖係本發明之局部分解之示意圖 第2圖係本發明之示意圖 第3圖係第2圖之Ⅲ-Ⅲ之示意圖 第4圖係第2圖之Ⅳ-Ⅳ之示意圖 第5A圖係本發明之排氣管部之第一實施例之示意圖 第5B圖係本發明之排氣管部之第二實施例之示意圖 第6圖係本發明之排氣管部之單排排氣口應用例之剖視圖 第7圖係本發明之排氣管部之雙排排氣口應用例之剖視圖 第8圖係本發明之氣泡供應部之示意圖 第9圖係本發明之電極殺菌部之示意圖 第10圖係本發明之設置複數個處理槽之示意圖 第11圖係本發明之處理方法之流程圖1 is a schematic view of a partial decomposition of the present invention, FIG. 2 is a schematic view of the present invention, FIG. 3 is a schematic view of III-III of FIG. 2, and FIG. 4 is a schematic view of FIG. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 5B is a schematic view showing a second embodiment of the exhaust pipe portion of the present invention. FIG. 6 is a view showing an application example of the single exhaust port of the exhaust pipe portion of the present invention. 7 is a cross-sectional view showing an application example of a double-row exhaust port of an exhaust pipe portion of the present invention. FIG. 8 is a schematic view showing a bubble supply portion of the present invention. FIG. 9 is a schematic view showing an electrode sterilization portion of the present invention. FIG. Schematic diagram of setting a plurality of processing tanks according to the present invention. FIG. 11 is a flow chart of a processing method of the present invention.

10‧‧‧控制部 10‧‧‧Control Department

20‧‧‧連續處理部 20‧‧‧Continuous Processing Department

21‧‧‧進水容納槽 21‧‧‧Intake tank

22‧‧‧電解殺菌槽 22‧‧‧ Electrolytic sterilization tank

221‧‧‧第一隔板 221‧‧‧ first partition

222‧‧‧第二隔板 222‧‧‧Second partition

223‧‧‧第三隔板 223‧‧‧ third partition

224‧‧‧第四隔板 224‧‧‧4th partition

225‧‧‧底部通口 225‧‧‧ bottom port

22A‧‧‧第一殺菌槽 22A‧‧‧First sterilization tank

22B‧‧‧第二殺菌槽 22B‧‧‧Second sterilization tank

22C‧‧‧第三殺菌槽 22C‧‧‧The third sterilization tank

23‧‧‧沉澱槽 23‧‧‧Sedimentation tank

24‧‧‧出水容納槽 24‧‧‧Water receiving tank

30‧‧‧電極殺菌部 30‧‧‧Electrode sterilization department

40‧‧‧氣泡供應部 40‧‧‧ Bubble Supply Department

42‧‧‧排氣管 42‧‧‧Exhaust pipe

421‧‧‧排氣口 421‧‧‧Exhaust port

50‧‧‧擾流部 50‧‧‧Surveying Department

91‧‧‧廢水 91‧‧‧ Wastewater

H1‧‧‧第一高度 H1‧‧‧ first height

H2‧‧‧第二高度 H2‧‧‧second height

Claims (6)

一種連續式之廢水的處理裝置,該處理裝置係設至少一個,該每一處理裝置包括:一控制部;一連續處理部,係連結該控制部,並具有依序相連通之一進水容納槽、一電解殺菌槽、一沉澱槽及一出水容納槽;其中,該進水容納槽係供一廢水流入;該出水容納槽係供該廢水流出;一電極殺菌部,係懸設於該電解殺菌槽內,並包括一正電極板、一負電極板、複數個介於其間且彼此不接觸之電感應極板;該控制部用以對該正電極板供應一正電,且該控制部係用以對該負電極板供應一負電;一氣泡供應部,係設於該電解殺菌槽內,且位於該電極殺菌部下方,該氣泡供應部係設一供氣裝置及至少一排氣管;該排氣管具有至少一排氣口;該控制部係連接該供氣裝置,用以控制該供氣裝置對該排氣管供入一空氣,該空氣經該至少一排氣口供入該電解殺菌槽內,用以於該廢水內形成複數個氣泡;一擾流部,係呈板狀結構,其一端懸設於沉澱槽其鄰近該出水容納槽的該端,且另端朝該電解殺菌槽的方向呈傾斜向下延伸;藉此,該廢水於流入再流出該連續處理部的過程中,且該電極殺菌部被供電時,係可與該廢水反應而產生次氯酸水,進而對該廢水產生殺菌作用,同時,該排氣口產生之複數個氣泡,係從該電解殺菌槽底部向上移動,移動過程可帶走該電解殺菌槽內相關結構上之污物,且該擾流部係使該廢水於該沉澱槽內先 呈反向渦流捲動後,方流入該出水容納槽,用以提高沉澱效果,達成連續式之廢水的處理裝置;其中:該排氣管係為複數支,且分別並列於該進水容納槽、該第一殺菌槽、該第二殺菌槽、該第三殺菌槽、該沉澱槽及該出水容納槽內;該排氣口係為孔結構、長條孔結構其中至少一者;該排氣口係設於該排氣管上,而為單排結構、雙排結構其中一者;並當為雙排結構,該兩排排氣口之間,係具有一工作角度;該處理裝置係設置複數個,且呈並聯。 A continuous wastewater treatment device, the treatment device is provided with at least one, each treatment device comprises: a control portion; a continuous treatment portion connected to the control portion and having one of the water inlets in sequence a tank, an electrolytic sterilization tank, a sedimentation tank and a water discharge tank; wherein the water inlet tank is for a wastewater to flow in; the water storage tank is for the wastewater to flow out; and an electrode sterilization portion is suspended in the electrolyte a positive electrode plate, a negative electrode plate, and a plurality of electric induction plates interposed therebetween and not in contact with each other; the control portion is configured to supply a positive power to the positive electrode plate, and the control portion The utility model is configured to supply a negative electricity to the negative electrode plate; a bubble supply portion is disposed in the electrolytic sterilization tank and located under the electrode sterilization portion, the air bubble supply portion is provided with a gas supply device and at least one exhaust pipe The exhaust pipe has at least one exhaust port; the control portion is connected to the air supply device for controlling the air supply device to supply an air to the exhaust pipe, and the air is supplied to the exhaust pipe through the at least one exhaust port In the electrolysis sterilization tank, use Forming a plurality of bubbles in the waste water; a spoiler portion having a plate-like structure, one end of which is suspended from the sedimentation tank adjacent to the end of the water discharge receiving tank, and the other end is inclined toward the electrolysis sterilization tank Lowering; thereby, the wastewater can be reacted with the wastewater to generate hypochlorous acid water during the process of flowing into the continuous processing portion, and the electrode sterilization portion is powered, thereby generating a bactericidal effect on the wastewater. At the same time, the plurality of bubbles generated by the exhaust port are moved upward from the bottom of the electrolysis sterilization tank, and the moving process can take away the dirt on the relevant structure in the electrolysis sterilization tank, and the spoiler part makes the wastewater Precipitation tank After being scrolled by the reverse vortex, it flows into the outlet tank to improve the sedimentation effect, and a continuous waste water treatment device is realized; wherein: the exhaust pipe is a plurality of branches, and are respectively juxtaposed in the water inlet tank The first sterilization tank, the second sterilization tank, the third sterilization tank, the sedimentation tank and the water outlet tank; the exhaust port is at least one of a hole structure and a long hole structure; the exhaust The mouth system is disposed on the exhaust pipe, and is one of a single row structure and a double row structure; and is a double row structure, the two rows of exhaust ports have a working angle; the processing device is set Multiple, and in parallel. 如申請專利範圍第1項所述之連續式之廢水的處理裝置,其中,該電解殺菌槽係包括一第一隔板、一第二隔板、一第三隔板及一第四隔板;其中,該第一隔板及該第二隔板係分別立設於該進水容納槽內,而隔離出該電解殺菌槽,該第一隔板具有一第一高度,該第二隔板具有一第二高度,其係低於該第一高度;該第三隔板係立設於該第一隔板與該第二隔板之間,而隔離出一第一殺菌槽;該第四隔板係懸設於該第一隔板及該第三隔板之間,而隔離出一第二殺菌槽及一第三殺菌槽,其間具有一底部通口;藉該第一殺菌槽、該第二殺菌槽、該底部通口及該第三殺菌槽,係可延長該廢水於該電解殺菌槽內被殺菌處理的時間。 The apparatus for processing a continuous type of waste water according to the first aspect of the invention, wherein the electrolysis sterilization tank comprises a first partition, a second partition, a third partition and a fourth partition; Wherein the first partition and the second partition are respectively disposed in the water inlet receiving groove to isolate the electrolytic sterilization tank, the first partition has a first height, and the second partition has a second height, which is lower than the first height; the third partition is erected between the first partition and the second partition to isolate a first sterilization tank; the fourth partition The plate system is suspended between the first partition plate and the third partition plate, and isolates a second sterilization tank and a third sterilization tank, and has a bottom opening; the first sterilization tank, the first The second sterilization tank, the bottom opening and the third sterilization tank can extend the time during which the wastewater is sterilized in the electrolytic sterilization tank. 如申請專利範圍第1項所述之連續式之廢水的處理裝置,其中,該出水容納槽係包括一主出水口及一副出水口,皆係用以供出殺菌處理後的該廢水。 The continuous waste water treatment device according to claim 1, wherein the water discharge tank comprises a main water outlet and a water outlet for supplying the waste water after the sterilization treatment. 一種連續式之廢水的處理方法,係包括下列步驟:一、準備步驟:係預先設置至少一個處理裝置,該每處理裝置係包括一控制部、一連續處理部、一電極殺菌部、一氣泡供應部及一擾流部;其中:該控制部係電性連結該電極殺菌部及該氣泡供應部,用以控制其動作;該連續處理部係連結該控制部,並具有依序相連通之一進水容納槽、一電解殺菌槽、一沉澱槽及一出水容納槽;該進水容納槽係供一廢水流入;該出水容納槽係供該廢水流出;該電極殺菌部係懸設於該電解殺菌槽內,並包括一正電極板、一負電極板、複數個介於其間且彼此不接觸之電感應極板;該氣泡供應部係設於該電解殺菌槽內,且位於該電極殺菌部下方,該氣泡供應部係設一供氣裝置及至少一排氣管;該排氣管係具有至少一排氣口;該控制部係連接該供氣裝置;該擾流部係呈板狀結構,其一端係懸設於沉澱槽其鄰近該出水容納槽的該端,且另端係傾斜向下而朝該電解殺菌槽的方向延伸;其中:該排氣管係為複數支,且分別並列於該進水容納槽、該第一殺菌槽、該第二殺菌槽、該第三殺菌槽、該沉澱槽及該出水容納槽內;該排氣口係為孔結構、長條孔結構其中至少一者;該排氣口係設於該排氣管上,而為單排結構、雙排結構其中一者;並當為雙排結構,該兩排排氣口之間,係具有一工作角度;該處理裝置係設置複數個,且呈並聯; 二、連續進水步驟:將該廢水連續供入該連續處理部;三、殺菌步驟:透過該控制部對該正電極板供應一正電,且透過該控制部對該負電極板供應一負電,則該廢水在流過該電極殺菌部的過程中,係可與該電極殺菌部反應而生成次氯酸水,進而對該廢水產生殺菌作用;四、氣泡擾動除污步驟:透過該控制部控制該供氣裝置對該排氣管供入一空氣,該空氣經該至少一排氣口供入該電解殺菌槽內,而形成從該電解殺菌槽底部向上移動的複數個氣泡,該每一氣泡於移動過程,除可擾動該廢水外,並可帶走該電解殺菌槽內相關結構上之污物;五、擾流除污步驟:該廢水從該電解殺菌槽流入該沉澱槽後,該擾流部係使該廢水於該沉澱槽內先呈反向渦流捲動後,方流入該出水容納槽,而不直接順向流入該出水容納槽,可用以提高沉澱效果;六、完成步驟:該廢水從該出水容納槽供出後,可供回收再利用。 A continuous waste water treatment method comprises the following steps: First, a preparation step: pre-setting at least one treatment device, wherein each treatment device comprises a control portion, a continuous treatment portion, an electrode sterilization portion, and a bubble supply And a spoiler; wherein: the control unit electrically connects the electrode sterilization unit and the bubble supply unit for controlling the operation thereof; the continuous processing unit is coupled to the control unit and has one of sequential connections a water inlet tank, an electrolytic sterilization tank, a sedimentation tank and a water discharge tank; the water inlet tank is for a waste water to flow; the water storage tank is for the waste water to flow; the electrode sterilization portion is suspended in the electrolysis a sterilizing tank includes a positive electrode plate, a negative electrode plate, and a plurality of electric induction plates interposed therebetween and not in contact with each other; the bubble supply portion is disposed in the electrolysis sterilization tank and located under the electrode sterilization portion The air supply unit is provided with a gas supply device and at least one exhaust pipe; the exhaust pipe system has at least one exhaust port; the control portion is connected to the air supply device; the spoiler portion is a plate-like knot One end of the sedimentation tank is suspended from the end of the water discharge receiving tank, and the other end is inclined downward to extend toward the electrolysis sterilization tank; wherein: the exhaust pipe is a plurality of branches, and are respectively juxtaposed In the water inlet receiving tank, the first sterilization tank, the second sterilization tank, the third sterilization tank, the sedimentation tank and the water outlet tank; the exhaust port is a hole structure and a long hole structure at least One of the exhaust ports is disposed on the exhaust pipe, and is one of a single row structure and a double row structure; and is a double row structure, the two rows of exhaust ports have a working angle The processing device is provided in plural and in parallel; a continuous water inflow step: continuously supplying the wastewater into the continuous processing portion; 3. a sterilization step: supplying a positive electricity to the positive electrode plate through the control portion, and supplying a negative electricity to the negative electrode plate through the control portion When the wastewater flows through the electrode sterilization unit, it can react with the electrode sterilization unit to generate hypochlorous acid water, thereby generating a bactericidal action on the wastewater. 4. The bubble disturbance decontamination step: through the control unit Controlling the air supply device to supply an air to the exhaust pipe, and the air is supplied into the electrolytic sterilization tank through the at least one exhaust port to form a plurality of air bubbles moving upward from the bottom of the electrolytic sterilization tank, each of the air bubbles In the moving process, in addition to disturbing the wastewater, the dirt on the relevant structure in the electrolysis sterilization tank may be taken away; 5. The turbulent decontamination step: after the wastewater flows into the sedimentation tank from the electrolysis sterilization tank, the disturbance The flow system causes the wastewater to be firstly swirled in the sedimentation tank and then flows into the outlet water receiving tank, and does not directly flow into the outlet water receiving tank, which can be used to improve the sedimentation effect; 6. Complete the steps: Waste Receiving water from the feed-out slot, for recycling. 如申請專利範圍第4項所述之連續式之廢水的處理方法,其中,該電解殺菌槽係包括:一第一隔板、一第二隔板、一第三隔板及一第四隔板,其中,該第一隔板及該第二隔板係分別立設於該進水容納槽內,而隔離出該電解殺菌槽,該第一隔板具有一第一高度,該第二隔板具有一第二高度,其係低於該第一高度;該第三隔板係立設於該第一隔板與該第二隔板之間,而產生一第一殺菌槽;該第四隔板係懸設於該第一隔板及該第三隔板之間,而隔離出一第二殺菌槽及一第三殺菌槽,其間具有一底部通口;藉該第一殺菌槽、該第二殺菌槽、該底部通口及該第三殺菌槽,係可延長該廢水於該電解殺菌槽內被殺菌處理的時間。 The method for treating a continuous type of wastewater according to claim 4, wherein the electrolytic sterilization tank comprises: a first partition, a second partition, a third partition, and a fourth partition. The first partition plate and the second partition plate are respectively erected in the water inlet receiving groove to isolate the electrolytic sterilization tank, the first partition plate has a first height, and the second partition plate has a first height Having a second height that is lower than the first height; the third partition is erected between the first partition and the second partition to produce a first sterilization tank; the fourth partition The plate system is suspended between the first partition plate and the third partition plate, and isolates a second sterilization tank and a third sterilization tank, and has a bottom opening; the first sterilization tank, the first The second sterilization tank, the bottom opening and the third sterilization tank can extend the time during which the wastewater is sterilized in the electrolytic sterilization tank. 如申請專利範圍第4項所述之連續式之廢水的處理方法,其中,該出水容納槽係包括一主出水口及一副出水口,皆係用以供出殺菌處理後的該廢水。The method for treating a continuous type of wastewater according to claim 4, wherein the effluent receiving tank comprises a main water outlet and a pair of water outlets for supplying the sterilized wastewater.
TW105137715A 2016-11-17 2016-11-17 Continuous waste water treatment device and treatment method TWI605020B (en)

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CN110734173A (en) * 2019-11-20 2020-01-31 北京丰舜通环保科技有限公司 electric flocculation oil-water separator

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Publication number Priority date Publication date Assignee Title
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