附件2a:第 851 1 1253 號專利申請案 387864 中文說明書修正頁_ 民國88年4月修正 五、發明說明（5 ) COD濃度： 3. 3公斤COD/立方米 pH: 7.1 回流淤泥濃度： 50克/升 ' 放流物中的B〇D5濃度：<4 5毫克/升 放流物中的固體含量：<· 50毫克/升 個別實_例 活化體稹（立方米） 活化室中的活性淤泥濃度 (克/升） 1516 12 1366 14 1271 16 圓式簡單說明 第1圖在於說明本發明方法的一項可能實施例，其中 之標號分別代表： (請先閱讀背面之注意事項再填寫本頁) 《I % ---------1^ 1 丨 I — I — II 1.λ 經濟部智慧財產局員工消费合作社印製 1 廢水 2 活化室 3 通氣 4 下流式反應器 5 浮選池 6 高壓水站 7 回流淤泥 8 過多淤泥 9 出口 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公爱） -8 - A7 ._B7 五、發明説明（！） 發明說明 本發明係有關一種廢水的生物處理方法，其中係將活 性淤泥和_廢水的混合物在活化階段中用氣體處理並將經活 化的淤泥從經處理的廢水浮選分離掉· 該類型方法已被揭示於例如德國專利申請第P 44 1 1 99 1. 7號中，其併於本文作爲參考 •於此類 經濟部中央標準局貝工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) 型的方法中，淤泥係與水力荷載該經處理的廢水·一起離 開活化階段，並在分離階段中經由浮選而從水力荷載分離 出且將其一部份循環回到活化階段以在活化階段中保持確 定之淤泥浪度*因爲這種操作方向之故，在活化階段中的 淤泥濃度與從分離階段中回流到活化階段_所謂回流淤泥的 排放物流中之撤_姆|1度_之間有一相關性。活化階段中的淤 泥濃度因而係由回流淤泥與幾乎無固體的廢水之混合物所 決定。以這種方法調定的活化階段中之淤泥濃度通常爲5 克/升（參看上述專利申請案）·該淤泥濃度在廢水生物 處理工廠的尺寸設計中是一項重要的參數，因其，則的不 說，可決定活化反應器的容稹，該容積會隨著淤泥濃度之 .遞增而遞減•所以可在相當髙淤泥濃度下操作的廢水處理 工廠若不具有某些嚴重缺點時將是所需求者。彼等工的缺 黏在於程序中的浮選分離部份，依淤泥濃度而定，必須做 得非常大，因而變成相應地非常地貴•再者*操作這類浮 選工廠會因其對廢水流速的變化有很敏感的反應而有困難 •此外，因爲浮選所需的高廢水流速與淤泥濃度有直接的 正比關係，而使其操作成本變得很高· 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公嫠） ] A7 _B7 五、發明説明（2 ) 頃令人訝異地發現若開頭所提類型的方法經修改成活 化階段中的活性淤泥濃度爲2 6克/升且該浮選係下文所 述類型的溶方式時，這些缺點即顯著地減低 〇 綜上所述，本發明係有關一種廢水生物處理方法，其 中將活性淤泥和廢水的混合物在活化階段中用氣體處理並 於活泥鈒經處埋水中浮離掉，其中該活化階 段中的活性淤泥濃度爲2 6克/升且其中該浮選爲溶解空 氣浮選•本發明方法的較佳實施例係由申請專利範圍第2 至3項所給· 本發明方法的第1較佳實施例爲在活化階段中的活性 淤泥濃度爲2 8克/升，較佳者2 1 0克/升，特別較佳 者2 1 2/升·另一較佳賁施例爲要進行浮選所用的懸浮 液係以S 0 . 3米/秒的流速被導引迎向氣泡上升的自然 經濟部中央標率局貝工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) 方向，於此情況中另外以氣體處理裝置用氣體處理該懸浮 液•經氣體處理的懸浮液係在該氣體處理裝置的底部取出 並給到浮選操作中*如德國專利申請案P 44 11 991. 7中所述者。 諸實施例中所提的諸特項中的個別特項或眾多特項也 可個別地構成本發明的解決之道，且也可以將個別特別依 窬要組合起來· 本發明方法的優點基本上在於廢水生物處理工廠的活 化階段和浮選階段都可做得比傳統廢水處理工廠都較爲小 •如此同時可改良其效率及簡化其操作。 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） 5 A7 _^_B7___ 五、發明説明（3 ) 本發明方法的一項可能之實施例要在下文參考附圔所 示程序流程圖予以更詳細地說明。 廢水_1係與稱爲回流淤泥7的活性淤泥在活化階段的 活化室2內混合並通氣3 ·於其過程中，廢水中所含污染 物即被生物分解掉。然後將淤泥和水的混合物通到一個垂 直直立下流式反應器4·於此作爲氣體處理裝置的下流式 反應器4之中，係將活性淤泥和水的混合物向下導引並於 其過程中予以通氣•必要時，可加入絮凝劑1 2 ·然後從 該下流式反應器4的底部取出該活性淤泥和水的混合物並 給對浮選池5之內，於其中將將活性淤泥從水中分離出來 •此項分離可以利用在髙壓水站6中游水和空氣1 0變成 高壓後釋放在浮選池5之內的作法予以加強•用於此作法 的水爲經純化的廢水1 1 *使用塔1 3作爲貯有槽•將分 離出的活性淤泥中的一部份作爲回流淤泥7循環回到活化 室2·其餘部份則以過多淤泥8之形式棄置掉•經純化過 的廢水係經由出口 9以經澄清化的水之形式取出· 本發明要用兩個操作例進一步解釋· 經濟部中央橾準局貝工消费合作社印裝 (請先聞讀背面之注意事項再填寫本頁) 該等實施例係有關廢水生物處理廠，其中係利用如上 所述的上游下流式塔經由溶解空氣浮選而分離出活性淤泥 •於生物處理的上游處，係對廢水進行初級澄清·於活性 淤泥濃度增加時，於各情況中對這些特殊廢水所形成的生 物團於分解動力學上沒有顯示出任何明顯的變化。針對分 廢水中所含個別成份的個別代謝程序而考慮對固體含量濃 度增加予以限制•於個別賁施例中’變異活化室的體積和 本紙張尺i逋用中國國家標隼（CNS ) Μ坑格（2〖0Χ297公釐） : 387864 A7 B7 五、發明説明（4 ] 活性淤泥濃度· 窗施例1 = 廢水特性和程序特性的數據如下： 3 0立方米/小時 2公斤B0D8/立方米 3. 4公斤COD/立方米 廢水流速 B 0 D β濃度： (生物窬氧量） C 0 D濃度： (化學窬氧量） pH: 6.8 回流淤泥濃度： 4 0克/升 放流物中的BOD5濃鍍：<45毫克/升 放流物中的固髋含量：<50毫克/升 個別實施例 活化體稹（立方米） 活化室中的活性淤泥濃度 (克/升） (請先閲讀背面之注意事項再填寫本頁) 經濟部中央橾準局貝工消费合作社印装 611 488 412 6 8 10 實施例2 廢水特性和程序特性的數據： 廢水流速 120立方米/小時 B0D5濃度： 2 . 2公斤Β Ο D 5/立方米 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） 7 附件2a:第 851 1 1253 號專利申請案 387864 中文說明書修正頁_ 民國88年4月修正 五、發明說明（5 ) COD濃度： 3. 3公斤COD/立方米 pH: 7.1 回流淤泥濃度： 50克/升 ' 放流物中的B〇D5濃度：<4 5毫克/升 放流物中的固體含量：<· 50毫克/升 個別實_例 活化體稹（立方米） 活化室中的活性淤泥濃度 (克/升） 1516 12 1366 14 1271 16 圓式簡單說明 第1圖在於說明本發明方法的一項可能實施例，其中 之標號分別代表： (請先閱讀背面之注意事項再填寫本頁) 《I % ---------1^ 1 丨 I — I — II 1.λ 經濟部智慧財產局員工消费合作社印製 1 廢水 2 活化室 3 通氣 4 下流式反應器 5 浮選池 6 高壓水站 7 回流淤泥 8 過多淤泥 9 出口 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公爱） -8 - 387864 五、發明説明（6 ) 1 0 空氣 1 1 經純化的廢水 1 2 絮凝劑 1 3 塔（貯存槽） -------r — ίό^I — (請先閲讀背面之注意事項再填寫本頁)Attachment 2a: Patent Application No. 851 1 1253 387864 Chinese Specification Revision Page _ Amendment in April of the Republic of China V. Description of Invention (5) COD concentration: 3.3 kg COD / m3 pH: 7.1 reflux sludge concentration: 50 g BOD5 concentration in the effluent: <4 5 mg / L solid content in the effluent: <50 mg / L individual case _ activated body 稹 (cubic meters) activated sludge in the activation chamber Concentration (g / l) 1516 12 1366 14 1271 16 Brief description of the circular type Figure 1 is a description of a possible embodiment of the method of the present invention, where the symbols represent: (Please read the precautions on the back before filling this page) "I% --------- 1 ^ 1 丨 I — I — II 1.λ Printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs 1 Wastewater 2 Activation chamber 3 Ventilation 4 Downflow reactor 5 Flotation cell 6 High-pressure water station 7 Returning sludge 8 Excessive sludge 9 Exit This paper size applies to Chinese National Standard (CNS) A4 (210 X 297 public love) -8-A7 ._B7 V. Description of the invention (!) The invention is related to Biological wastewater treatment method The mixture of sludge and wastewater is treated with gas in the activation stage and the activated sludge is separated from the treated wastewater flotation. This type of method has been disclosed, for example, in German Patent Application No. P 44 1 1 99 1. 7 It is also used as a reference in this article. • In the method printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page), the sludge system and hydraulic load should be The wastewater leaves the activation stage together, and is separated from the hydraulic load by flotation in the separation stage, and a part of it is recycled back to the activation stage to maintain the determined sludge wave length during the activation stage * because of the direction of this operation Therefore, there is a correlation between the concentration of the sludge in the activation phase and the withdrawal from the separation phase to the activation phase—the so-called reflux sludge discharge stream—1 degree. The sludge concentration in the activation stage is therefore determined by the mixture of the returning sludge and the almost solid-free wastewater. The sludge concentration in the activation phase set by this method is usually 5 g / liter (see the above patent application). The sludge concentration is an important parameter in the size design of the wastewater biological treatment plant. Not to mention, the capacity of the activation reactor can be determined, and the volume will decrease as the concentration of the sludge increases. Therefore, a wastewater treatment plant that can be operated at a considerable concentration of sludge will have no serious disadvantages. requester. The lack of viscosity of their workers lies in the flotation separation part of the process. Depending on the concentration of the sludge, it must be made very large, and accordingly becomes very expensive. Changes in the flow rate have a very sensitive response and are difficult. In addition, the high wastewater flow rate required for flotation has a direct proportional relationship with the concentration of sludge, which makes its operating cost very high. This paper scale applies Chinese national standards ( CNS) A4 specification (210X297 gong)] A7 _B7 V. Description of the invention (2) It is surprisingly found that if the method of the type mentioned at the beginning is modified to an activated sludge concentration of 26 g / l in the activation stage and When the flotation system is a type of dissolution method described below, these disadvantages are significantly reduced. In summary, the present invention relates to a biological wastewater treatment method in which a mixture of activated sludge and wastewater is treated with a gas in the activation stage And floated off in the buried water of live loach, where the activated sludge concentration in the activation stage was 26 g / L and where the flotation was dissolved air flotation • a preferred implementation of the method of the present invention It is given by items 2 to 3 of the scope of patent application. The first preferred embodiment of the method of the present invention is that the activated sludge concentration in the activation stage is 28 g / l, preferably 210 g / l, particularly The better is 2 1 2 / liter. Another preferred embodiment is that the suspension used for flotation is guided at a flow rate of S 0.3 m / s toward the central standard of the Ministry of Natural Economy. Printed by the local shellfish consumer cooperative (please read the precautions on the back before filling this page). In this case, the gas treatment device is used to treat the suspension with gas. The gas treated suspension is in the gas treatment device. The bottom is removed and given to the flotation operation * as described in German patent application P 44 11 991.7. Individual features or features among the features mentioned in the embodiments can also individually constitute the solution of the present invention, and individual special dependencies can also be combined. The advantages of the method of the present invention are basically The wastewater biological treatment plant's activation stage and flotation stage can be made smaller than traditional wastewater treatment plants. In this way, it can improve its efficiency and simplify its operation. This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 5 A7 _ ^ _ B7___ V. Description of the invention (3) One possible embodiment of the method of the present invention is to refer to the program flow chart shown in the appendix below Explain in more detail. Wastewater_1 is mixed with aerated sludge called reflux sludge 7 in the activation chamber 2 of the activation stage and aerated 3. In the process, the pollutants contained in the wastewater are biodegraded. The mixture of sludge and water is then passed to a vertical upright reactor 4. The downflow reactor 4 which is used as a gas treatment device is used to guide the mixture of activated sludge and water downward and in the process. Ventilation • If necessary, a flocculant 1 2 can be added. Then the active sludge and water mixture is taken out from the bottom of the downflow reactor 4 and fed into the flotation cell 5 where the active sludge is separated from the water. Out • This separation can be enhanced by the method of releasing water and air 10 from the pressurized water station 6 into high pressure and releasing it into the flotation cell 5. • The water used for this method is purified wastewater 1 1 * Use Tower 1 3 serves as a storage tank. • A part of the separated activated sludge is recycled to the activation chamber 2 as reflux sludge. 7 The rest is discarded as excessive sludge. • The purified wastewater is passed through The outlet 9 is taken out in the form of clarified water. The present invention will be further explained by two operating examples. Printed by the Shellfish Consumer Cooperative of the Central Bureau of Quasi-Ministry of Economic Affairs (please read the precautions on the back before filling out this page). Wait The example is related to a biological wastewater treatment plant, in which the activated sludge is separated by dissolved air flotation using an upstream downflow tower as described above. At the upstream of the biological treatment, the primary clarification of the wastewater is performed. The activated sludge concentration increases. In each case, the biomass formed by these special wastewaters did not show any obvious change in the decomposition kinetics. Consider the restriction of the increase of the solid content concentration for the individual metabolic process of the individual components contained in the wastewater. • In the individual examples, the volume of the mutation activation chamber and the paper rule are in accordance with the Chinese National Standard (CNS). Grid (2 〖0 × 297mm）: 387864 A7 B7 V. Description of the invention (4) Activated sludge concentration · Window Example 1 = The data of wastewater characteristics and program characteristics are as follows: 3 0 cubic meters / hour 2 kg B0D8 / cubic meters 3 4 kg COD / m3 wastewater flow rate B 0 D β concentration: (biological oxygen) C 0 D concentration: (chemical oxygen) pH: 6.8 reflux sludge concentration: 40 g / l BOD5 concentration in the effluent Plated: < 45 mg / L solids content in release fluid: < 50 mg / L Individual Example Activator (cubic meter) Active Sludge Concentration (g / L) in Activation Chamber (Please read the back Please fill in this page again for attention) Printed by the Central Bureau of Standards and Quarantine, Shellfish Consumer Cooperative, 611 488 412 6 8 10 Example 2 Data of wastewater characteristics and process characteristics: Wastewater flow rate 120 cubic meters / hour B0D5 concentration: 2.2 kg Β Ο D 5 / m3 paper size Applicable to China National Standard (CNS) A4 specification (210X297 mm) 7 Annex 2a: Patent Application No. 851 1 1253 387864 Chinese Manual Correction Page _ Amendment in April of the Republic of China 5. Description of Invention (5) COD concentration: 3. 3 kg COD / m3 pH: 7.1 reflux sludge concentration: 50 g / l 'BOD5 concentration in the effluent: < 4 5 mg / l solid content in the effluent: < 50 mg / l individual solid _Example of activated slugs (cubic meters) Concentration of activated sludge in the activation chamber (g / l) 1516 12 1366 14 1271 16 Circular brief description Figure 1 is a description of a possible embodiment of the method of the present invention, where the numbers are Representative: (Please read the precautions on the back before filling this page) "I% --------- 1 ^ 1 丨 I — I — II 1.λ Printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs 1 Wastewater 2 Activation chamber 3 Ventilation 4 Downflow reactor 5 Flotation cell 6 High-pressure water station 7 Returning sludge 8 Excessive sludge 9 Exit This paper applies Chinese national standard (CNS) A4 specifications (210 X 297 public love) -8-387864 V. Description of the invention (6) 1 0 Air 1 1 Purified Wastewater 1 2 flocculant 1 3 tower (storage tank) ------- r — ίό ^ I — (Please read the precautions on the back before filling this page)
_-1T 經濟部中央標準局爲工消费合作社印製 本紙張尺度逋用中國圃家橾準（CNS ) Α4現格（210X297公釐）_-1T Printed by the Central Bureau of Standards of the Ministry of Economic Affairs for the Industrial and Consumer Cooperatives. This paper is in Chinese standard (CNS) A4 (210X297 mm).