TW585841B - Sewage treatment system - Google Patents

Sewage treatment system Download PDF

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TW585841B
TW585841B TW89104564A TW89104564A TW585841B TW 585841 B TW585841 B TW 585841B TW 89104564 A TW89104564 A TW 89104564A TW 89104564 A TW89104564 A TW 89104564A TW 585841 B TW585841 B TW 585841B
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tank
sewage
aeration
water
digestion
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TW89104564A
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Chinese (zh)
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Ping-Ren Wu
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Yi Entpr Co Ltd Di
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  • Biological Treatment Of Waste Water (AREA)

Abstract

The present invention provides a sewage treatment method and system. The invented method uses a biological treatment and comprises: (a) introducing sewage into an adjustment tank for adjusting the pH value of the sewage contained therein and the amount of sewage contained; (b) introducing the sewage from the adjustment tank to a decomposition tank in order to reduce the BOD and COD of the sewage; (c) introducing the sewage from the decomposition tank to a contact aeration tank to perform a digestion and nitrogen-removal treatment; (d) introducing the sewage treated in step (c) to an anaerobic fermentation sedimentation tank to perform an anaerobic decomposition and sewage sedimentation treatment, as well as an aeration reduction treatment in order to further ferment the residual matter in the sewage; and (e) discharging the sewage treated in step (d) in a digestion tank for further treatments in order to remove the impurities in water by oxy-reduction processes.

Description

585841 A7 ____B7_ 五、發明說明(/ ) 發明領域 本發明係關於一種污水處理方法及其系統,其係利用 生物處理使污水在處理之後,其水質可達國家放流標準, 並且不會產生污泥排放處理之問題。 發明背景 在一般傳統污水處理系統於環工微生物之運用上,大 都使用固定式生物濾膜,或是以廢水與接觸材料上生長生 物膜接觸,進而達到污水處理的效果。使用此種固定式生 物膜之污水處理,一般來說,傳統污水處理系統中之反應 膜,因缺乏循環的功能,而以自然腐化的方式進行初步分 解,以致污泥沉澱之情形相當嚴重。另一方面,因爲傳統 污水處理系統中之反應槽,其生長趨勢達到死亡期時,會 導致微生物活性及其系統能量降低,而促進大量膠羽的形 成,造成污泥二次來源。 因此,需要一種符合國家放流標準,亦不會產生污泥 二次來源之新穎的污水處理方法及其系統。 發明摘述 因此,本發明之目的係提供一種污水處理方法及其系 統,其係利用生物處理,在沒有使用任何化學或加藥方式 處理之下,使污水於處理後,其水質達到國家放流標準, 避免化學藥劑造成二次公害及污泥排放處理之問題的產生 0 爲達到上述之目的,提供一種根據本發明之污水處理 方法,其包括: 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁)585841 A7 ____B7_ V. Description of the Invention (/) Field of the Invention The present invention relates to a sewage treatment method and system, which uses biological treatment to make sewage after treatment, and its water quality can reach the national discharge standard, and no sludge discharge will occur. Deal with the problem. BACKGROUND OF THE INVENTION In the application of conventional traditional sewage treatment systems to environmental workers, most of them use fixed biofiltration membranes, or contact wastewater with biofilms grown on contact materials, thereby achieving the effect of sewage treatment. Wastewater treatment using such fixed biofilms. Generally speaking, the reaction membranes in traditional sewage treatment systems lack natural circulation and are preliminarily decomposed in a natural decay manner, resulting in a serious situation of sludge sedimentation. On the other hand, when the growth trend of the reaction tank in the traditional sewage treatment system reaches the death stage, it will cause the reduction of microbial activity and its system energy, and promote the formation of a large number of rubber plumes, causing a secondary source of sludge. Therefore, there is a need for a novel wastewater treatment method and system that meets national discharge standards and does not generate secondary sources of sludge. SUMMARY OF THE INVENTION Therefore, the object of the present invention is to provide a sewage treatment method and a system thereof, which use biological treatment without any chemical or medicinal treatment, so that after the treatment, the water quality reaches the national discharge standard To avoid the secondary pollution caused by chemical agents and the problem of sludge discharge treatment. 0 In order to achieve the above-mentioned purpose, a sewage treatment method according to the present invention is provided, which includes: The paper size is applicable to the Chinese National Standard (CNS) A4 specification ( 210 X 297 mm) (Please read the notes on the back before filling this page)

585841 A7 ______B7__ 五、發明說明(> ) (a) 將污水引入一調節槽中調節其pH値及水量; (b) 將來自調節槽之放流水引入一分解槽中,其中生物 宿材培養特殊自然酵素寄居於其中,以使污水經過生物宿 材以降低水中之BOD與COD ; (c) 將來自分解槽之放流水引入一接觸曝氣槽中,其 中設有一種超微曝氣設備,可使污水同時進行消化及脫氮 9 (d) 將來自步驟(C)之放流水引入一喜厭發酵沉澱槽中 ’於槽中具有一隔層,使槽之底層可進行厭氧分解及污泥 沉澱’槽之上隔層可進行曝氣還原以再度發酵水中之殘餘 物質; (e) 於一消化槽中,將來自步驟(d)之放流水進一步處理 ,以消除水中的雜質還原氧化。 根據本發明之方法,其進一步在步驟(c)中,包括一將 污泥回抽至調節槽中,以增加處理效果。 再者,提供一種根據本發明之污水處理系統,其包括 (a) —調節槽,其係用於調節污水之pH値及水量; (b) —分解槽,其利用寄居於生物宿材上之酵素降低 水中之BOD與COD ; (c) 一接觸曝氣槽,其中設有一種超微曝氣設備,可 使污水進行消化脫氮; (d) —喜厭發酵沉澱槽,槽中具有一隔層,於槽之底 層可進行厭氧分解及污泥沉澱,槽之上隔層可進行曝氣還 -----5___ 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公爱) (請先閱讀背面之注意事項再填寫本頁)585841 A7 ______B7__ V. Description of the invention (&); (a) The sewage is introduced into a regulating tank to adjust its pH 値 and water volume; (b) The discharge water from the regulating tank is introduced into a decomposition tank, in which the biological material culture is special Natural enzyme resides in it, so that the sewage passes through the biological material to reduce BOD and COD in the water; (c) The discharge water from the decomposition tank is introduced into a contact aeration tank, which is equipped with an ultra-micro aeration device, which can Simultaneous digestion and denitrification of sewage 9 (d) The release water from step (C) is introduced into a anaerobic fermentation sedimentation tank with a partition in the tank, so that the bottom of the tank can undergo anaerobic decomposition and sludge The compartment above the sedimentation tank can be subjected to aeration reduction to re-ferment the residual material in the water; (e) in a digestion tank, further treating the effluent water from step (d) to eliminate the reduction and oxidation of impurities in the water. According to the method of the present invention, further in step (c), a method of pumping the sludge back to the adjusting tank to increase the treatment effect is provided. Furthermore, a sewage treatment system according to the present invention is provided, which includes (a) an adjustment tank, which is used to adjust the pH of the sewage and the amount of water; (b), a decomposition tank, which uses Enzymes reduce BOD and COD in water; (c) a contact aeration tank, which is equipped with an ultra-micro aeration device, which can digest and denitrify sewage; (d) a hi-fermentation fermentation tank, with a partition in the tank Layer, the bottom of the tank can be anaerobic decomposition and sludge sedimentation, the compartment above the tank can be aerated also ----- 5___ This paper size applies to China National Standard (CNS) A4 specifications (210 X 297 public love ) (Please read the notes on the back before filling this page)

585841 A7 ___ B7__ 五、發明說明(多) 原以再度發酵水中之殘餘物質;及 (e) —消化槽,其係用於消除水中的雜質還原氧化。 根據本發明之系統,其進一步在消化槽之後,包括一 微曝放流槽。 根據本發明之系統,其進一步在喜厭發酵沉澱槽中設 有污泥回抽設備。 圖式簡單說明 第1圖是根據本發明之污水處理系統的圖式; 圖式元件符號說明 (請先閱讀背面之注意事項再填寫本頁) 1 曝氣管 2 生物宿材 3 曝氣機 4 回抽泵浦 5,7 隔層 6 三角架 8 調節槽 9 分解槽 10 接觸曝氣槽 11 喜厭發酵沉澱槽 12 消化槽 13 微曝放流槽 14 污水入口 15 放流口 -ϋ H ϋ n n I n^-OJ I I I ϋ n n n I I 一 ^---------------------- 本纸張尺度適用中國國家標準(CNS)A4規格(21〇 X 297公釐) 585841 A7 ___ B7___ 五、發明說明(f ) 發明說明 本發明之生物污水處理方法及其系統之主要原理是基 於,在反應槽中具有功能不同之數種以上的微生物附著於 生物宿材上,並在曝氣管之存在下,經由曝氣管之適當的 放置及所產生之循環對流情形,可於反應槽中產生模擬自 然之環境區域。此模擬之生態系可分爲對流區域(含氧量較 高之區)、反應槽角落處無產生對流區域(幾乎沒有含氧量) 至其兩區交接邊緣處的區域處(含氧量高於反應槽角落處微 生物群最佳之生存環境),讓不同之微生物能對碳水化合物 進行呼吸作用或發酵作用,做進一步的消化。因此,在本 發明之生物處理方式的方法中,只要污水經過便產生大量 菌體群,其中,例如桿菌及球菌擔任特殊分解作用。因其 具有宿居作用,故不易隨水排放,因此其功能相當穩定而 且持久,此一污水處理方式,將污染的有機物污水作全面 淨化處理,所以無污泥的二度污染。 本發明所利用之生物處理方式具有下列之作用: 1·培植對環境有益性生物群,不具毒性,對人、畜無 害、無腐蝕性,安全無慮。 2·槽中設有超微曝設備,具氣提作用會充分攪拌污水 ’而具有超高溶解酸素效率,並可抑制腐敗菌生長,促進 發酵菌之繁殖。 3·槽中自然產生適應其環境的微好氧性及極小型通氣 嫌氣性菌,因無大型好氧菌,所以幾乎沒有污泥。 4·單位面積微生物量多,生物相亦多。 ____7__________ 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁)585841 A7 ___ B7__ 5. Description of the invention (many) Residual substances in water were originally fermented again; and (e)-digestion tank, which is used to eliminate the reduction and oxidation of impurities in water. The system according to the present invention further includes a micro-exposure drain tank after the digestion tank. According to the system of the present invention, it is further provided with a sludge re-pumping device in the anaerobic fermentation sedimentation tank. Brief description of the drawings The first diagram is the diagram of the sewage treatment system according to the present invention; Symbols of the diagram elements (please read the precautions on the back before filling this page) 1 Aeration pipe 2 Biological sink material 3 Aerator 4 Pump back 5,5 Shelf 6 Tripod 8 Regulating tank 9 Decomposition tank 10 Contact aeration tank 11 Fermentation fermentation sedimentation tank 12 Digestion tank 13 Micro-aeration drain tank 14 Sewage inlet 15 Drain port -ϋ H ϋ nn I n ^ -OJ III ϋ nnn II One ^ ---------------------- This paper size applies to China National Standard (CNS) A4 (21〇X 297) (Centi) 585841 A7 ___ B7___ 5. Description of the invention (f) Description of the invention The main principle of the biological wastewater treatment method and system of the present invention is based on the fact that in the reaction tank, several or more microorganisms with different functions are attached to the biological material. In the presence of the aeration tube, through the proper placement of the aeration tube and the resulting circulation convection, a natural environment area can be created in the reaction tank. The simulated ecosystem can be divided into convection areas (areas with high oxygen content), no convection areas at the corners of the reaction tank (almost no oxygen content), and areas at the junction of the two areas (high oxygen content) The best living environment for the microbiota at the corner of the reaction tank), so that different microorganisms can breathe or ferment carbohydrates for further digestion. Therefore, in the method of the biological treatment method of the present invention, as long as the sewage passes through, a large number of bacterial groups are generated, among which, for example, bacilli and cocci play a special decomposition role. Because of its residential effect, it is not easy to discharge with water, so its function is quite stable and durable. This sewage treatment method comprehensively purifies the polluted organic sewage, so there is no secondary pollution of sludge. The biological treatment method used in the present invention has the following effects: 1. Cultivation is beneficial to the environmentally beneficial biomes, non-toxic, harmless to humans and animals, non-corrosive, and safe. 2. The tank is equipped with ultra-micro exposure equipment, which has a gas-lifting effect and will agitate the wastewater sufficiently, and has super high dissolving acid efficiency, and can inhibit the growth of spoilage bacteria and promote the reproduction of fermentation bacteria. 3. Micro-aerobic and extremely small-scale aerobic bacteria that naturally adapt to their environment are produced in the tank. There are no large-scale aerobic bacteria, so there is almost no sludge. 4. There are many microorganisms per unit area and there are many biological phases. ____7__________ This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) (Please read the precautions on the back before filling this page)

585841 A7 _;____B7___ 五、發明說明(Γ ) 5·可有效去除生物分解性或分解速率低的基質。 6·兼具好氧厭氧作用。 參照所附之圖式,本發明之污水處理方法及其系統, 係利用前述之生物處理的原則,將污水依序經由下列各個 單元的處理,以達到國象排放標準,並無污泥處理之產生 1·調節槽(8):其係用於接收污水並調節其水質pH及 水量; 2·分解槽(9):本槽爲曝氣分解槽,本槽生物宿材(2) 培養特殊自然酵素寄居於其中,污水經過生物宿材(2)後能 降低水中之COD與BOD,本槽處理之效率是以附著在生 物宿材(2)表面之自然酵素所產生之薄膜爲主,其反應如下 0.02〜〇.〇35m3/m3-min 大於 min0.06m3/m3 0.026 〜0.033kw/m3 3.接觸曝氣槽(10): 在本槽中設有一種超微曝氣設備,其在槽中可產生下 述功能: (1) 充分攪拌污水並使其產生自然酸解素° (2) 超音波作用以轉換自然生物酶。 (3) 使其具有硝化脫氮之功能。 (4) 產生大量有益菌種於自然界中。 本槽中之生物處理的反應機制係如下所示 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁)585841 A7 _; ____B7___ V. Description of the invention (Γ) 5. It can effectively remove the matrix with low biodegradability or low decomposition rate. 6. Both aerobic and anaerobic effects. Referring to the attached drawings, the sewage treatment method and system of the present invention use the aforementioned biological treatment principles to sequentially treat sewage through the following units to achieve the national elephant discharge standards, and there is no sludge treatment. Generate 1 · Adjustment tank (8): It is used to receive sewage and adjust its water quality pH and water volume; 2 · Decomposition tank (9): This tank is an aeration decomposition tank, and the biological material in this tank (2) special and natural cultivation The enzyme resides in it. The sewage can reduce the COD and BOD in the water after passing through the biological material (2). The efficiency of this tank treatment is mainly based on the thin film produced by the natural enzyme attached to the surface of the biological material (2). The following 0.02 ~ .35m3 / m3-min is greater than 0.06m3 / m3 0.026 ~ 0.033kw / m3 3. Contact aeration tank (10): An ultra-micro aeration device is set in this tank, which is in the tank It can produce the following functions: (1) Stir the sewage sufficiently to produce natural acidolysin ° (2) Ultrasound to convert natural biological enzymes. (3) Make it have the function of nitrification and denitrification. (4) Produce a large number of beneficial bacteria in nature. The reaction mechanism of biological treatment in this tank is shown below. The paper size is applicable to Chinese National Standard (CNS) A4 (210 X 297 mm) (Please read the precautions on the back before filling this page)

585841 A7 B7 五、發明說明(4 ) 氧 脫氮一Ν2 厭氧生物Β 好氧生物層初層I— -Οι (空氣) J ·—有機物(BOD)水中 --C〇2+H2〇+能量 均S有機酸 4.喜厭發酵沉澱槽(11): (1) 本槽用特殊酵素,培植在生物宿材(2)中,於槽中做 一隔層(7),在底層無氧氣狀態下,經由厭氧分解並可做污 泥沉澱槽之功能,以經由厭氧分解成爲穩定水質,其原理 如下: CNHa〇b+(n-a/4-b/2)H2〇 — (n/2-a/8+b/4)C〇2+(n/2+a/8-b/4)CH4 (2) 本槽之上隔層則進行曝氣還原,使水中殘餘之物質 再度發酵,揮發在空氣中。其反應公式如下: CaHbNd +f〇2-m^ nCwHx〇yN2+mCH4+sC〇2+yH2〇 5·消化槽(12): 本槽以特殊培養配合自然酵素充分的接觸混合以消除 水中的雜質還原氧化,並使水質中COD、BOD、S.S降低 在國家標準指數內。 根據本發明之上述的處理流程,其進一步可在消化槽 (12)之後,包括一微曝放流槽(13),以作爲放流水及檢測水 — _____9 _ 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁) |-------訂-------l· -線 —, 585841 A7 B7 五、發明說明(7 ) 質用。 根據本發明之上述處理流程,其進一步在喜厭發酵沉 澱槽中設有污泥回抽設備(句,將污泥回抽至調節槽中以增 加處理效果。 在前述所提之生物宿材(2)可爲具有下列特性: a) 木質纖維不規則鉅齒狀; b) 具中空纖維束管; c) 具耐水性及耐腐性;及 d) 具半懸浮性。 爲論證本發明之可實施性,並具有產業上利用之價値 ,茲參照所附之圖式,並以下實施例作爲印證: 實施例: 將來自,例如化糞池污水或生活污水的7.5噸/日污水 量,250人使用人數,及具有下表1之水質狀況污水送入 前述之生物污水處理系統中。 表1原污水之水質狀況 pH 5-9 BOD 250mg/L 以上 COD 250mg/L 以上 s.s 250mg/L 以上 大腸桿菌 105個以上/毫升 表2爲顯示用於施行本發明之污水處理系統,各處_ 槽之尺寸,及所含之生物宿材及酵素之使用量。 (請先閱讀背面之注意事項再填寫本頁)585841 A7 B7 V. Description of the invention (4) Oxygen denitrification-N2 Anaerobic B Beta aerobic biological layer I--〇ι (air) J ·-organic matter (BOD) water-C〇2 + H2〇 + energy All S organic acids 4. Hi-fermentation fermentation sedimentation tank (11): (1) This tank uses special enzymes to be cultivated in biological materials (2), and a compartment (7) is formed in the tank, and the bottom layer is free of oxygen. It can be used as a sludge sedimentation tank through anaerobic decomposition to stabilize water quality through anaerobic decomposition. The principle is as follows: CNHa〇b + (na / 4-b / 2) H2〇— (n / 2-a / 8 + b / 4) C〇2 + (n / 2 + a / 8-b / 4) CH4 (2) The upper compartment of this tank is subjected to aeration reduction, so that the remaining substances in the water are fermented again and volatilized. in the air. The reaction formula is as follows: CaHbNd + f〇2-m ^ nCwHx〇yN2 + mCH4 + sC〇2 + yH205 · Digestive tank (12): This tank uses special culture and natural enzymes to make full contact mixing to eliminate impurities in the water Reduction and oxidation, and reducing the COD, BOD, and SS in water quality within the national standard index. According to the above-mentioned processing flow of the present invention, it may further include a micro-exposure drain tank (13) after the digestion tank (12) for draining water and testing water — _____9 _ This paper standard is applicable to Chinese National Standards (CNS) A4 specifications (210 X 297 mm) (Please read the precautions on the back before filling out this page) | ------- Order ------- l · -Line—, 585841 A7 B7 V. Invention Note (7) Quality. According to the above-mentioned treatment process of the present invention, it is further provided with a sludge suction pumping device (sentence, sludge is pumped back to the adjustment tank to increase the treatment effect in the anaerobic fermentation sedimentation tank. In the aforementioned biological material ( 2) It can have the following characteristics: a) Irregular megatooth shape of wood fiber; b) With hollow fiber bundle tube; c) Water resistance and corrosion resistance; and d) Semi-suspension. In order to demonstrate the feasibility of the present invention and its value for industrial use, please refer to the attached drawings, and use the following examples as proof: Examples: 7.5 tons from, for example, septic tank sewage or domestic sewage The daily sewage volume, 250 users, and sewage with the water quality status of Table 1 below are sent to the aforementioned biological sewage treatment system. Table 1 Water quality of raw sewage pH 5-9 BOD 250mg / L or more COD 250mg / L or more ss 250mg / L or more E. coli 105 or more / ml Table 2 shows the sewage treatment system for implementing the present invention, everywhere_ The size of the tank, and the amount of biological materials and enzymes used. (Please read the notes on the back before filling this page)

^ I— m i^i ί» i m «^1 一一口,I ϋ HI an n I in in I 線丨# f— — — — —— — —— — — — — — — — —— — — — 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 585841 Α7R7 表2 五、發明說明(?) 槽體名稱 調節槽 (8) 分解槽 (9) 接觸曝氣槽(10) 喜厭發 酵沉澱 槽(11) 消化槽 (12) 微曝放 流槽 (13) 合計 1室 2室 有效容積 fm3) 7.92 3.955 2.61 1.74 2.8125 1 1.1 20.1375 有效水深 (m) 2 2 1.8 1.8 1.8 1.2 1.2 15.8 曝氣管 ⑴(支) 4 2 1 1 1 2 1 12 基本風量 (L/min) 160 80 40 40 40 40 20 420 曝氣機(3) SPP-200 (台) 2 抽水泵浦 (4)(台) 1 二角架 (6)(個) 4 2 1 1 1 2 1 13 生物宿材 (2)(公升) 1190 390 130 60 50 1820 酵素 (公升) 7 4 2 3 1 17 其中該曝氣管(1)可爲具有下述之尺寸及材質: a) —管狀直徑約67公厘,長度約570公厘(實際散氣 長度約500公厘); b) 圓周均勻佈滿約1公厘之孔隙,孔數約10080孔; 及 c) 支撐管外徑約63公厘,厚度約3公厘之硬質PVC 材質。 其中該曝氣管係固定在三角架(6)上,並距離槽底1〇 公分,且曝氣管之間距係隨面積大小而配置。所使用之曝 氣機(3)爲電磁式馬達,110V電壓,出風量爲200L/min以 下,噪音値低於50分貝。 本紙張尺度適用中國國家標準(CNS)A4規格(210 χ 297公釐) (請先閱讀背面之注意事項再填寫本頁) -------^--------- 585841 A7 ---B7 五、發明說明(7 ) 下表3所示爲處理後之水質狀況 表3 pH 6-9 BOD 80mg/L COD 80mg/L S.S 80mg/L 腸桿菌 3000個/毫升 由上表3中之數據可知,污水在經由本發明之污水處 理方法及其系統處理之後,確實可明顯降低污水中BOD、 COD、S.S及大腸桿菌數以達到國家放流水排放管制標準 ,並且沒有污泥處理之問題產生。 上述所揭示之圖式及說明僅爲本發明之實施例’其並 非是用來限定本發明。對於熟於此技藝者’可根據上述之 說明而進行等效變化及修飾’而該等變化及修飾均應涵 在本文所附之申請專利範圍之範疇內。 _____12 本纸張尺度適用中國國家標準(CNS)A4規格(21〇 X 297公釐) (請先閱讀背面之注意事項再填寫本頁) |-------訂-------Γ線!^ I— mi ^ i ί »im« ^ 1 One bite, I ϋ HI an n I in in I line 丨 # f — — — — — — — — — — — — — — — — — — This paper size applies to Chinese National Standard (CNS) A4 (210 X 297 mm) 585841 Α7R7 Table 2 5. Description of the invention (?) Tank name adjustment tank (8) Decomposition tank (9) Contact aeration tank (10) Fermentation and sedimentation tanks (11) Digestion tanks (12) Micro-exposure bleed tanks (13) Total effective volume of 1 and 2 chambers fm3) 7.92 3.955 2.61 1.74 2.8125 1 1.1 20.1375 Effective water depth (m) 2 2 1.8 1.8 1.8 1.2 1.2 15.8 Aeration pipe 支 (branch) 4 2 1 1 1 2 1 12 Basic air volume (L / min) 160 80 40 40 40 40 20 20 420 Aerator (3) SPP-200 (set) 2 Pump (4) ( Units) 1 Corner frame (6) (pieces) 4 2 1 1 1 2 1 13 Biological materials (2) (liters) 1190 390 130 60 50 1820 Enzymes (liters) 7 4 2 3 1 17 Wherein the aeration tube (1) It can have the following dimensions and materials: a)-tube diameter of about 67 mm, length of about 570 mm (actual air diffusion length of about 500 mm); b) uniform circumference of about 1 mm The porosity, pore holes of approximately 10,080; and c) a support tube diameter of approximately 63 mm, a thickness of about 3 mm of rigid PVC material. The aeration tube is fixed on a tripod (6) and is 10 cm away from the bottom of the tank, and the distance between the aeration tubes is configured according to the area. The aerator (3) used is an electromagnetic motor, with a voltage of 110V, an air output of 200L / min or less, and a noise level of less than 50dB. This paper size applies to China National Standard (CNS) A4 (210 χ 297 mm) (Please read the precautions on the back before filling this page) ------- ^ --------- 585841 A7 --- B7 V. Description of the invention (7) The following table 3 shows the water quality after treatment. Table 3 pH 6-9 BOD 80mg / L COD 80mg / L SS 80mg / L Enterobacter 3000 pcs / ml from the table above According to the data in 3, after the sewage is treated by the sewage treatment method and system of the present invention, the number of BOD, COD, SS, and E. coli in the sewage can be obviously reduced to meet the national discharge water discharge control standard, and there is no sludge treatment. Problems arise. The drawings and descriptions disclosed above are merely examples of the present invention, and are not intended to limit the present invention. For those skilled in this art, 'equivalent changes and modifications can be made according to the above description', and such changes and modifications should be included in the scope of the patent application attached hereto. _____12 This paper size applies to China National Standard (CNS) A4 (21〇X 297 mm) (Please read the notes on the back before filling this page) | ------- Order ------ -Γ line!

Claims (1)

585841 A8 C8 D8 六、申請專利範圍 中該生物宿材包括木屑/ (0 —用於接收來自分解槽之放流水以使污水進行消化 脫氮之接觸曝氣槽,其中該曝氣槽具有一種超微曝氣設備 ,以使污水進行消化脫氮,其中該超微曝氣設備爲一種具 有數千至上萬的1公厘微小孔而能產生微小氣泡之曝氣管 (d) —用於接收來自接觸曝氣槽之放流水的喜厭發酵沉 澱槽,於槽中具有一隔層,槽之底層進行厭氧分解與污泥 沉澱,槽之上隔層進行曝氣還原以再度發酵水中之殘餘物 質;及 (e) —用來將來自喜厭發酵沉澱槽之放流水作進一步處 理的消化槽,以消除水中的雜質還原氧化。 4. 根據申請專利範圍第3項之系統,其進一步在消化 槽之後,包括一微曝放流槽。 5. 根據申請專利範圍第3項之系統,其中喜厭發酵沉 澱槽具有污泥回抽設備。 2 (請先閲讀背面之注意事項再填寫本頁) 訂: ^^^用中國國家標準(CNS)A^規格(21〇χ 297公釐)585841 A8 C8 D8 6. In the scope of the patent application, the biological material includes sawdust / (0—a contact aeration tank for receiving discharged water from a decomposition tank for digestion and denitrification of sewage, wherein the aeration tank has a super Micro-aeration equipment for digestion and denitrification of sewage, wherein the ultra-microaeration equipment is an aeration tube (d) with thousands of to tens of thousands of 1mm micropores and capable of generating microbubbles—for receiving from The anaerobic fermentation sedimentation tank contacting the discharged water of the aeration tank has a partition in the tank. The bottom layer of the tank is subjected to anaerobic decomposition and sludge sedimentation, and the top layer of the tank is subjected to aeration to reduce the remaining substances in the fermentation water And (e)-a digestion tank for further processing the effluent water from the anaerobic fermentation sedimentation tank to further reduce oxidation of impurities in the water. 4. The system according to item 3 of the scope of patent application, which is further in the digestion tank After that, a micro-exposure bleed tank is included. 5. According to the system of patent application No. 3, the hi-fermentation sedimentation tank has a sludge pumping device. 2 (Please read the notes on the back before filling Page) Order: ^^^ with China National Standard (CNS) A ^ Specifications (21〇χ 297 mm)
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI386375B (en) * 2005-09-09 2013-02-21 Net Co Ltd Biological processing mehtod and apparatus for organic sewage

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI386375B (en) * 2005-09-09 2013-02-21 Net Co Ltd Biological processing mehtod and apparatus for organic sewage

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