完整後設資料紀錄
DC 欄位 | 值 | 語言 |
---|---|---|
dc.contributor.author | 蔡承祐 | en_US |
dc.contributor.author | Tsai, Cheng-Yu | en_US |
dc.contributor.author | 林志高 | en_US |
dc.contributor.author | Lin, Jih-Gaw | en_US |
dc.date.accessioned | 2014-12-12T02:44:43Z | - |
dc.date.available | 2014-12-12T02:44:43Z | - |
dc.date.issued | 2014 | en_US |
dc.identifier.uri | http://140.113.39.130/cdrfb3/record/nctu/#GT070151728 | en_US |
dc.identifier.uri | http://hdl.handle.net/11536/76060 | - |
dc.description.abstract | 相較於傳統好氧活性污泥法處理污水,厭氧生物處理不僅耗能少還具有產生能源的潛力,因此,已被廣泛應用於處理不同種類的廢水。然而,厭氧生物處理啟動時間較長是其缺點之一,成為限制其實廠化的主要限制因素。本研究利用高效率厭氧流體化床反應槽結合厭氧流體化薄膜反應槽 (AFBR-AFMBR) 在室溫下處理都市污水,目的在探討利用沸石作為載體所需的啟動時間及反應槽表現,及評估利用此系統處理低濃度生活污水之可行性。本研究以1000 mg COD/L合成廢水、水力停留時間 (HRT) 為1 d、有機負荷率 (OLR) 為1 g/m3/d,以半連續模式操作啟動階段。系統操作到第32天,pH值維持在7,化學需氧量 (COD) 去除效率達90%以上,穩定後的產氣量為1 L/d,顯示系統已達穩定。且揮發性懸浮固體物濃度 (VSS) 從100 降至10 mg/L。另外,在室溫 (20 to 35oC) 連續模式操作下處理低濃度真實污水 (73 to 220 mg COD/L),總化學需氧量去除率達70到90%、總懸浮性固體物去除率達96%及0.13 L CH4/g CODremoved之比甲烷產量。且薄膜在薄膜通量10 LMH下操作333天,不須經化學清洗。除此之外,系統所需之總能量僅0.015 kWh/m3,又產生之甲烷可提供能量約0.0024 kWh/m3。以上結果皆顯示厭氧流體化床反應槽結合厭氧流體化薄膜反應槽 (AFBR-AFMBR) 能成功應用在處理低濃度生活污水。 | zh_TW |
dc.description.abstract | In the present study, an anaerobic fluidized bioreactor combined with an anaerobic fluidized membrane bioreactor (AFBR-AFMBR) was used to for treat municipal wastewater at ambient temperature. The objectives of this study were to evaluate the start-up time and the performance using zeolite as carriers and the performance of the AFBR-AFMBR. During the start-up period, the reactor system was operated in semi-continuous mode and at a hydraulic retention time (HRT) of 1 d and an organic loading rate (OLR) of 1 g/m3/d with influent chemical oxygen demand (COD) of 1000 mg COD/L (made by synthetic wastewater). The reactor system reached to steady state with a pH level of 7, COD removal efficiency higher than 90% and 1 L/d of the steady biogas production. The microorganisms were successfully attached onto the carrier. Thereafter, the reactor system was changed to continuous mode operation at 3.5 h of total HRT for treating municipal wastewater (73 to 220 mg COD/L) at ambient temperature ranged from 20 to 35oC. The reactor performance reached to 70 to 90% of COD removal, 96% of total suspended solids (TSS) removal and 0.13 L CH4/g CODremoved of specific methane production. The membrane module in AFMBR can be continuously used for 333 d at a flux of 10 LMH without chemical cleaning. Besides, the reactor system only needed 0.015 kWh/m3 of pumping energy requirement and can generate 0.0024 kWh/m3 of methane energy. The above results revealed that the AFBR-AFMBR is a high efficiency energy-saving system for treating municipal wastewater. | en_US |
dc.language.iso | en_US | en_US |
dc.subject | 厭氧流體化床反應槽 | zh_TW |
dc.subject | 生活污水 | zh_TW |
dc.subject | anaerobic fluidized bioreactor | en_US |
dc.subject | municipal wastewater | en_US |
dc.title | 利用AFBR-AFMBR系統處理台灣低濃度生活污水 | zh_TW |
dc.title | Start-up and performance evaluation of the AFBR-AFMBR system treating low-strength municipal wastewater in Taiwan | en_US |
dc.type | Thesis | en_US |
dc.contributor.department | 環境工程系所 | zh_TW |
顯示於類別: | 畢業論文 |