527326 A7 B7 五、 、發明説明 (1 ) [ 發 明 領 域 1 本 發 明 是有 關 於 一 種 處 理 系 統 5 特 別 是 指 一 種 處 理 速 度 快 不 佔 用 空 間 之 廢 水 處 理 系 統 〇 [ 習 知 技 藝 說 明 ] 一 般 塗 料 粉 塵 的 捕 集 設 備 主 要 是 利 用 集 塵 裝 置 作 處 理 處 理 方 式 分 成 乾 式 及 濕 式 〇 針 對 乾 式 之 處 理 9 是 在 集 塵 室 (罩) 以 風 車 的 抽 吸 作 用 , 抽 取 空 氣 中 的 雜 質 9 進 入 一 過 濾 箱 攔 截 固 體 成 份 直 到 濾 材 飽 和 之 後 , 再 將 該 廢 棄 物 丟 棄 惟 > 處 理 後 的 廢 棄 物 並 無 法 再 回 收 而 轉 變 成 二 次 污 染 〇 針 對 濕 式 之 處 理 與 乾 式 類 同 , 但 濕 式 不 使 用 濾 材 而 是 使 用 水 洗 方 式 將 固 成 份 攔 截 下 來 再 加 混 凝 劑 沈 澱 變 成 廢 棄 物 丟 棄 0 以 上 乾 濕 兩 種 處 理 方 式 並 無 法 直 接 作 有 效 的 回 收 濾 材 及 濾 水 只 能 視 同 廢 棄 物 丟 棄 因 此 , 存 在 有 廢 棄 垃 圾 廢 水 • · · 等 衍 生 的 問 題 , 仍 無 法 有 效 解 決 〇 以 濕 式 處 理 而 言 雖 缺 可 利 用 添 加 混 凝 劑 使 固 體 沈 澱 後 再 行 處 理 但 是 , 一 般 作 法 其 處 理 的 空 間 要 很 大 亦 即 5 處 理 廢 水 的 佔 地 要 很 廣 才 足 夠 處 理 , 因 此 9 便 造 成 以 往 處 理 系 統 之 成 本 昂 且 處 理 速 度 慢 • * · 等 業 界 一 直 以 來 無 法 突 破 的 缺 失 〇 [ 發 明 概 要 ] 因 此 5 本 發 明 之 a 的 即 在 提 供 一 種 處 理 速 度 快 不 佔 用 空 間 且 可 降 低 成 本 之 廢 水 處 理 系 統 〇 於 是 ’ 本 發 明 之廢水處理系統( 么含: 有, 廢 水 處 理 單 第 3 頁 訂 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 請 丨丨 先 ; 閲 _ 讀 ; 背 : ^ · 之 丨 意丨 事: 項 : 再 卜 fm 本: 頁: 527326 A7 B7 五、 、發明説明 (2 ) 元 具 有 利 用 一 供 水 泵 浦 白 一 污 水 池 中 吸 入 廢 水 , 在 吸 入 管 内 加 入 中 和 劑 後 泵 入 一 第 一 混 合 攪 拌 桶 5 利 用 管 内 廢 水 為 動 力 ,使 中 和 劑 與 廢 水 充 分 混 合 後 ,經由- 一 PH 偵 測 電 極 偵 測 酸 驗 值 ,之 遂加 空 氣 ,進入該供水泵# f加壓攪拌, 使 廢 水 與 空 氣 充 分 混 合 並 產 生 大 量 微 小 氣 泡 ’ 經 過 一 纏 繞 在 一 浮 除 槽 的 壓 力 溶 氣 管 呈 渦 流 狀 態 送 再 使 產 生 微 小 氣 泡 的 廢 水 經 一 定 量 喷 嘴 以 較 小 的 口 徑 喷 出 廢 水 , 並 加 入 混 凝 劑 送 入 一 第 二 混 合 攪 拌 桶 充 分 混 合 攪 拌 再 經 過 一 纏 繞 在 該 浮 除 槽 的 凝 聚 反 應 管 呈 /1¾ 流 狀 態 之 送 j 使 廢 水 中 之 懸 浮 物 質 呈 凝 聚 狀 5 加 入 助 凝 劑 使 廢 水 中 的 雜 質 適 度 凝 結 再 送 入 該 浮 除 槽 y 此 時 , 廢 水 中 呈 混 凝 狀 態 的 雜 質 , 受 到 大 量 溶 解 在 廢 水 中 微 小 氣 泡 之 浮 昇 效 應 , 便 飄 浮 到 該 浮 除 槽 頂 部 ;的i 1 α , 1經過- -位於該 出 α 頂 部 的 刮 除 機 將 污 泥 廢 棄 物 逐 漸 刮 除 9 且 由 一 污 泥 輸 送 流 道 流 送 出 去 5 而 沈 積 在 該 浮 除 槽 底 部 的 淨 水 經 排 放 管 排 出 便 可 回 收 再 利 用 〇 [ 圖 式 之 簡 單 說 明 ] 本 發 明 之 其 他 特 徵 及 優 點 在 以 下 配 合 參 考 圖 式 之 較 佳 實 施 例 的 詳 細 說 明 中 將 可 清 楚 的 明 白 在 圖 式 中 : 第 一 圖 是 一 側 視 圖 說 明 本 發 明 之 廢 水 處 理 系 統 的 一 較 佳 實 施 例 9 第 二 圖 是 該 廢 水 處 理 系 統 的 一 頂 視 圖 f 第 三 圖 是 一 正 視 圖 , 說 明 一 自 動 控 制 系 統 一 加 藥 泵 浦 及 一 儲 藥 桶 的 組 合 狀 態 9 第 4 頁 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 527326 A7 —________B7 五、發明説明(3 ) 請 先 閲 讀 背 之 注 意 事 項 再 填 寫 本 頁 第四圖是該廢水處理系統的一控制流程圖;及 第五圖是一立體圖,說明一浮除槽清除污泥的狀態。 【較佳實施例之詳細說明】 如第一圖所示,本發明之廢水處理系統1的一較佳實施 例疋包含一廢水處理單元1 〇、一藥劑供給單元2 0及一廢棄 物收集單元3 〇。 如第一、二、四圖所示,該廢水處理單元1 〇具有利用 一供水泵浦1 1 ( 1 〇 1 )自一污水池4 〇中吸入廢水,在吸入管内 加入中和劑後(1 〇 2 ),泵入一第一混合攪拌桶1 2 ( 1 0 3 ),利 用管内廢水為動力,使中和劑與廢水充分混合後,經由一 ^偵測電極1 3偵測酸鹼值(丨〇 4 ),之後,加入空氣或 〇 (1 〇 5 ),進入該供水泵浦丨丨加壓攪拌(丨〇 6),使廢水與空 氧充刀展合並產生大量微小氣泡,經過一纏繞在一浮除槽 1 4外部的壓力溶氣管丨5的渦流輸送,該壓力溶氣管丨5是由 上往下纏繞在該浮除槽丨4底段。再使產生微小氣泡的廢水 經一定量噴嘴1 5 1以較小的口徑噴出廢水,加入混凝劑 (1〇8) 並送入一第二混合擾拌桶1 6充分混合授拌(1 〇 9 ), 再經過一纏繞在浮除槽丨4的凝聚反應管丨7之渦流輸送 (1 1 0 )’使廢水中之懸浮物質呈凝聚狀,該凝聚反應管】7 是由上往下纏繞在該壓力溶氣管丨5外部。並加入助凝劑 (1 1 1 )’再送入該浮除槽1 4 (1 1 2 ),此時,如第五圖所示, 廢水中呈混凝狀態的雜質,受到大量溶解在廢水中微小氣 泡之浮昇效應,便飄浮到該浮除槽14頂部的出口 141,經過 一位於該出口 1 4 1頂部的刮除機1 8,利用一馬達1 8丨轉動一 第5頁 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 527326 五’ 組刮 送流 管排 藥機 該泡 經由 制該 助凝 路之 該污 集桶 收集 物, 一壓 泥塊 集滿 脫水 統會 啟動 用清 開一 A7 B7 發明説明(4 ) 板1 8 2將污泥廢棄物1 0 0逐漸刮除(1 1 3 ),且由一污泥輸 道1 4 2流送出去,而沈積在浮除槽1 4底部的淨水經排放 出,便可回收再利用。 如第一、二、三圖所示,該藥劑供給單元2 0具有一泡 2 1、一自動控制系統2 2、三加藥泵浦2 3及三儲藥桶2 4, 藥機2 1包括預泡製各種化學藥劑,藥劑泡製完成後, 人工將藥劑加入儲藥桶2 4,再由該自動控制系統2 2控 等加藥泵浦2 3,使該儲藥桶2 4的一中和劑藥桶2 4 1、一 劑藥桶2 4 2及一混凝劑藥桶2 4 3中的藥劑,經由不同管 連接並以定量泵浦(圖未示)定量供給各藥劑。 如第一、二圖所示,該廢棄物收集單元30具有二位於 泥輸送流道1 4 2底部的污泥收集桶3 1、一位於二污泥收 1 3 1之間的轉轴3 2、及一污泥壓縮裝置3 3。其中一污泥 桶3 1位該於污泥輸送流道1 4 2底部提供集收污泥廢棄 另一污泥收集桶3 1位於該污泥壓縮裝置3 3底部,利用 桿3 3 1末端的一壓盤3 3 2將污泥廢棄物1 0 0壓縮脫水呈 狀。當位於該污泥輸送流道1 4 2底部的污泥收集桶3 1 時,經由轉軸3 2旋轉至該污泥壓縮裝置3 3底部供壓縮 如第二圖所示,該廢水處理單元1開始運作之前,該系 先執行一次自動操作模式,該自動操作模式係在自動 之後,開啟一位於該壓力溶氣管1 5出口的清洗閥1 5 2, 水清洗管路約三分鐘,接著將該清洗閥1 5 2關閉,並打 位於該凝聚反應管1 7出口的回水閥1 7 1,加入中和劑、 第6頁 本紙張尺度適用中國國家標準(CNS) Α4規格(210X297公釐) 請 先 閲 讀 背 之 注 意 事 項527326 A7 B7 V. Description of the Invention (1) [Field of the Invention 1 The present invention relates to a treatment system 5 especially to a waste water treatment system that has a fast processing speed and does not take up space. [Description of Known Skills] General Dust Capture The collection equipment mainly uses the dust collection device for processing. It is divided into dry type and wet type. For the dry type treatment 9 is the suction effect of the windmill in the dust collection room (hood). The impurities in the air are extracted 9 into a filter box to intercept the solids After the components are saturated with the filter material, the waste is discarded. However, the treated waste cannot be recycled and is converted into secondary pollution. The wet treatment is similar to the dry type, but the wet type does not use the filter material but uses it. Water washing method will intercept the solid content and add coagulant precipitation to become waste Disposal of waste above 0. Wet and dry treatment methods cannot be directly used for effective recovery. Filter media and water can only be discarded as waste. Therefore, there are problems caused by waste garbage and waste water, etc., which cannot be effectively solved. Although there is a lack of coagulant treatment, the solids can be treated by adding a coagulant. However, in general, the space for treatment is large, that is, the land area for the treatment of waste water is wide enough to be treated, so 9 has caused the past. The cost of the processing system is high and the processing speed is slow. * * Such a defect that the industry has been unable to break through. [Summary of the invention] Therefore, 5a of the present invention is to provide a waste water treatment system that has a fast processing speed without occupying space and can reduce costs. 〇So 'the wastewater treatment system of the present invention ( Yes, page 3 of the waste water treatment sheet paper size is applicable to Chinese National Standard (CNS) A4 (210X297 mm) Please 丨 first; read _ read; memorize: ^ · its 丨 meaning 丨 matter: item: again fm This: Page: 527326 A7 B7 V. Description of the invention (2) Yuan has the use of a water supply pump to pump waste water into the white sewage tank, and after adding a neutralizing agent into the suction pipe, it is pumped into a first mixing tank 5 using the waste water in the pipe As a motive force, after the neutralizer and the waste water are sufficiently mixed, the acid value is detected through a pH detection electrode, and air is then added to the water pump #f to pressurize and stir, so that the waste water and air are fully mixed and a large amount of water is generated. Micro-bubbles' are sent in a vortex state through a pressure-dissolved gas pipe wound in a floating removal tank, and then the wastewater that generates micro-bubbles is ejected through a certain number of nozzles with a smaller diameter, and the coagulant is added to a The second mixing and stirring bucket is fully mixed and stirred, and then sent through a coagulation reaction tube wound in the floatation tank in a state of 1¾ to make the suspended matter in the wastewater appear to be agglomerated. 5 The addition of a coagulant aid makes the impurities in the wastewater moderately coagulate Then it is sent to the floating tank y. At this time, the impurities in the coagulated state in the wastewater are floated to the top of the floating tank due to the floating effect of a large number of tiny bubbles dissolved in the wastewater; i 1 α, 1 passes through-- The scraper at the top of the outlet α gradually scrapes the sludge waste 9 and sends it out through a sludge conveying channel 5 and the clean water deposited on the bottom of the floatation tank is discharged through the discharge pipe and can be recycled and reused. 〇 [Simplified description of the drawings] Other features and advantages of the present invention will be clearly understood in the following detailed description of the preferred embodiments with reference to the drawings. In the drawings: the first diagram is a side view illustrating a preferred embodiment 9 of the wastewater treatment system of the present invention, the second diagram is a top view of the wastewater treatment system, and the third diagram is a front view illustrating an automatic control System combination status of a dosing pump and a medicine storage barrel 9 Page 4 This paper size applies Chinese National Standard (CNS) A4 (210X297 mm) 527326 A7 —________ B7 V. Description of the invention (3) Please read the back first Please note that the fourth figure is a control flow chart of the wastewater treatment system; and the fifth figure is a perspective view illustrating the state of sludge removal by a floating removal tank. [Detailed description of the preferred embodiment] As shown in the first figure, a preferred embodiment of the wastewater treatment system 1 of the present invention includes a wastewater treatment unit 10, a medicine supply unit 20, and a waste collection unit. 3 〇. As shown in the first, second, and fourth figures, the wastewater treatment unit 10 has the capability of sucking wastewater from a sewage tank 40 using a water supply pump 11 (100), and adding a neutralizing agent (1 〇2), pumped into a first mixing tank 12 (103), using the wastewater in the tube as a power to make the neutralizer and wastewater fully mixed, through a detection electrode 1 3 to detect the pH value (丨 〇4), after that, add air or 〇 (105), enter the water supply pump 丨 丨 pressurize and stir (丨 〇6), make the wastewater and air oxygen filling knife merge to generate a lot of fine bubbles, after a winding The vortex conveying of a pressure-dissolved gas pipe 丨 5 outside a floating tank 14 is wound around the bottom section of the floating-water tank 4 from top to bottom. Then, the wastewater that generates micro-bubbles is sprayed with a small diameter through a certain number of nozzles 151, and the coagulant (108) is added and sent to a second mixing and stirring tank 16 for full mixing and mixing (1 〇). 9), and then passed through a coagulation reaction tube 丨 4 vortex conveying (1 1 0) 'wound in the floatation tank 丨 4 to make the suspended matter in the waste water agglomerate, the coagulation reaction tube] 7 is wound from top to bottom Outside the pressure dissolving gas pipe 5. Add coagulant (1 1 1) 'and send it to the floating tank 1 4 (1 1 2). At this time, as shown in the fifth figure, the impurities in the coagulated state in the wastewater are largely dissolved in the wastewater. The floating effect of the tiny bubbles floats to the outlet 141 on the top of the floating tank 14 and passes through a scraper 18 on the top of the outlet 1 4 1 and uses a motor 1 8 丨 to rotate a page 5 paper size Applicable to China National Standard (CNS) A4 specification (210X297 mm) 527326 Five-slot scraper flow tube medicine discharge machine The bubble passes through the sewage collection barrels that make the coagulation assisting path, and a pressure mud block fills the dehydration union A7 B7 is used for start-up. Description of the invention (4) The board 1 8 2 gradually scrapes the sludge waste 1 0 0 (1 1 3), and it is sent out by a sludge channel 1 4 2 and deposited in The purified water at the bottom of the floating tank 14 can be recycled for reuse. As shown in the first, second, and third figures, the medicine supply unit 20 has a bubble 2 1, an automatic control system 2 2, three dosing pumps 23, and three medicine storage buckets 24. The medicine machine 21 includes Various chemicals are pre-baked. After the brewing is completed, the medicine is manually added to the medicine storage bucket 2 4 and then controlled by the automatic control system 22 to wait for the dosing pump 2 3 to make one of the medicine storage bucket 2 4 The medicines in the medicine tank 2 4 1, the medicine tank 2 4 2 and the coagulation medicine tank 2 4 3 are connected through different pipes and are dosed by a dosing pump (not shown). As shown in the first and second figures, the waste collection unit 30 has two sludge collection buckets 3 located at the bottom of the mud conveying channel 1 4 2 and a rotating shaft 3 2 located between the two sludge collection 1 3 1 And a sludge compression device 3 3. One of the sludge buckets 3 is located at the bottom of the sludge conveying channel 1 4 2 to collect and collect sludge and discard the other sludge collection bucket 3 1 is located at the bottom of the sludge compression device 3 3. A pressure plate 3 3 2 compresses and dewaters the sludge waste 100 into a shape. When the sludge collection bucket 3 1 at the bottom of the sludge conveying channel 1 4 2 is rotated to the bottom of the sludge compression device 3 3 via the rotating shaft 32 for compression as shown in the second figure, the wastewater treatment unit 1 starts Before the operation, the department first performed an automatic operation mode. After the automatic operation, the cleaning valve 1 5 2 at the outlet 15 of the pressure gas pipe was opened, and the water washes the pipeline for about three minutes, and then the cleaning was performed. The valve 1 5 2 is closed, and the return water valve 1 7 1 at the outlet of the condensation reaction tube 17 is added, and a neutralizer is added. Page 6 This paper applies the Chinese National Standard (CNS) A4 specification (210X297 mm) Read the notes first
頁 訂 頁 527326 A7 B7 五、發明説明(5 ) 打入空氣及加入混凝劑,而管内未加空氣的水 4 0,回水的時間約三分鐘,最後,再關閉該回; 開啟一位於該凝聚反應管1 7的供水閥1 7 2,再加 可。 另外,當加入中和劑之後,經由該PH偵測 P Η值的酸鹼值若不符合預設值時,該自動控制 動彳貞得’事先經人為設定’並適時控制劑量之 混凝劑、該助凝劑的添加量亦同,該藥劑供給 供一正確劑量的藥劑,使處理廢水達到環保標 歸納上述,本發明之廢水處理系統1經過各 處理,以及加入空氣或03,及加壓供水,使廢 並產生大量微小氣泡,經過渦旋式的壓力溶氣 反應管1 7的處理之後,以不佔空間的方式完成 廢棄物,最後,再經過該浮除槽1 4在大量氣泡 污泥可快速浮出,並受該刮除機1 8刮除,沈留 水可放流或回收再利用,污泥則經過壓縮脫水 發明之廢水處理系統1不僅處理速度快,且不佔 可降低成本,故確實能達到發明之目的。 惟以上所述者,僅為本發明之较佳實施例 能以此限定本發明實施之範圍,即大凡依本發 範圍及發明說明書内容所作之簡單的等效變化 應仍屬本發明專利涵蓋之範圍内。 第 本紙張尺度適用中國國家標準(CNS) Α4規格(210X297公釐) 排回污水池 表閥1 7 1,並 入助凝劑即 電極1 3偵測 系統2 2會自 增減,而該 單元20可提 準之條件。 步驟的藥劑 水充分溶解 管1 5及凝聚 混合、凝結 浮昇之下, 於底部的淨 ,因此,本 用空間,亦 而已,當不 明申請專利 與修飾,皆 527326 A7 B7 五、發明説明(6 ) 【元 件 標 號 對 照 I 本案 部 份 ; 1 廢 水 處 理 系 統 10 廢 水 處 理 單 元 11 供 水 泵 浦 12 第 一 混 合 攪 拌 桶 13 PH值 偵 測 電 極 14 浮 除 槽 141 出 口 142 污 泥 送 流 道 15 壓 力 溶 氣 管 151 定 量 喷 嘴 152 清 洗 閥 16 第 二 混 合 攪 拌 桶 17 凝 聚 反 應 管 171 回 水 閥 172 供 水 閥 18 刮 除 機 181 馬 達 182 刮 板 20 藥 劑 供 給 單 元 21 泡 藥 機 22 白 動 控 制 系 統 23 加 藥 泵 浦 24 儲 藥 桶 241 中 和 劑 藥 桶 242 助 凝 劑 藥 桶 243 混 凝 劑 藥 桶 30 廢 棄 物 收 集 〇 口 一 早兀 31 污 泥 收 集 桶 32 轉 軸 33 污 泥 壓 縮 裝 置 331 壓 桿 332 壓 盤 100 污 泥 廢 棄 物 第8頁 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐)Page ordering page 527326 A7 B7 V. Description of the invention (5) Inject air and add coagulant, and the water without air in the tube 40, the return time is about three minutes, and finally, close the back; The water supply valve 17 2 of the condensation reaction tube 17 is added. In addition, after the neutralizer is added, if the pH value of the PΗ value detected by the pH does not meet the preset value, the automatic control can be 'pre-set by man' and the dose of the coagulant is controlled in a timely manner. The addition amount of the coagulant is the same. The medicament is supplied for a correct dose of medicament, so that the treated wastewater reaches the environmental protection standard. The above-mentioned, the wastewater treatment system 1 of the present invention undergoes various treatments, and is added with air or 03, and pressurized. Supply water to make waste and generate a lot of tiny air bubbles. After treatment by vortex pressure dissolved gas reaction tube 17, the waste is completed in a space-free manner. Finally, the floatation tank 14 passes through a large number of air bubbles. The sludge can quickly float out and be scraped by the scraper 18. The sunken water can be discharged or recycled for reuse. The sludge is processed by the wastewater treatment system 1 which is invented by compression and dehydration. It can really achieve the purpose of invention. However, the above are only the preferred embodiments of the present invention, which can limit the scope of implementation of the present invention, that is, simple equivalent changes made in accordance with the scope of the present invention and the contents of the description of the invention should still be covered by the patent of the present invention. Within range. This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm). It is discharged back to the septic tank meter valve 1 7 1 and incorporated into the coagulant aid electrode 1 3 detection system 2 2 will automatically increase or decrease, and the unit 20 Conditions that can be cited. The medicine water in the step fully dissolves the tube 15 and condenses and mixes, condenses and floats, and it is cleaned at the bottom. Therefore, the space used here is just that, when unknown patents and modifications are applied, both 527326 A7 B7 V. Description of the invention (6 ) [Comparison of component numbers I Part of this case; 1 Wastewater treatment system 10 Wastewater treatment unit 11 Water supply pump 12 First mixing tank 13 PH detection electrode 14 Flotation tank 141 Outlet 142 Sludge flow channel 15 Pressure dissolving gas pipe 151 Dosing nozzle 152 Cleaning valve 16 Second mixing tank 17 Condensation reaction tube 171 Return valve 172 Water supply valve 18 Scraper 181 Motor 182 Scraper 20 Medicine supply unit 21 Medicine dispenser 22 White motion control system 23 Dosing pump 24 Medicine barrels 241 Neutralizer barrels 242 Coagulant barrels 243 Coagulant barrels 30 Waste collection 0 mouth early morning 31 Sludge collection barrels 32 Rotating shafts 3 3 Sludge compression device 331 Pressure rod 332 Pressure plate 100 Sludge waste and waste Page 8 This paper size applies to China National Standard (CNS) A4 (210X297 mm)