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| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 林正芳 | |
| dc.contributor.author | Yu-Lin Hsu | en |
| dc.contributor.author | 許瑜玲 | zh_TW |
| dc.date.accessioned | 2021-05-20T20:10:15Z | - |
| dc.date.available | 2019-12-31 | |
| dc.date.available | 2021-05-20T20:10:15Z | - |
| dc.date.copyright | 2009-08-11 | |
| dc.date.issued | 2009 | |
| dc.date.submitted | 2009-07-29 | |
| dc.identifier.citation | . A Joint Committee of the Water Pollution Control Federation and the American Society of Civil Engineers, 1977. Wastewater treatment plant design. Lancaster Press, Lancaster, PA.
Iwai, S., Kitao, T., 1994. Wastewater treatment with microbial films. Technomic Publishing Company, Lancaster, PA. Mattok, G., 1978. New processes of waste water treatment and recovery. Ellis Horwood Limited, Sussex, England. Vesilind, P.A., 2003. Wastewater treatment plant design. Water Environment Federation, London, UK. Water Environment Federation, American Society of Civil Engineers, 1991. Design of wastewater treatment plants. American Society of Civil Engineers, Brattleboro, Vermont. Chang, C.T., Chen, B.Y., Shiu, I.S., Jeng, F.T., 2004. Biofiltration of trimethylamine-containing waste gas by entrapped mixed microbial cells. Chemosphere 55, 751-756. Cho, E.S., Zhu, J., Yang, P.Y., 2007. Intermittently aerated EMMC-Blobarrel (entrapped mixed microbial cell with Bio-barrel) process for concurrent organic and nitrogen removal. Journal of Environmental Management 84, 257-265. Ghyoot, W., Verstraeth, W., 1999. Reduced sludge production in a two-stage membrance-assisted bioreactor. Water Res. 34, 205-215. Heran, M., Wisniewski, C., Orantes, J., Grasmick, A., 2008. Measurement of kinetic parameters in a submerged aerobic membrane bioreactor fed on acetate and operated without biomass discharge. Biochemical Engineering Journal 38, 70-77. Ichinari, T., Ohtsubo, A., Ozawa, T., Hasegawa, K., Teduka, K., Oguchi, T., Kiso, Y., 2008. Wastewater treatment performance and sludge reduction properties of a household wastewater treatment system combined with an aerobic sludge digestion unit. Process Biochemistry 43, 722-728. Kim, S.J., Yang, P.Y., 2004. Two-stage entrapped mixed microbial cell process for simultaneous removal of organics and nitrogen for rural domestic sewage application. Water Science and Technology 49, 281-288. Kim, S.J., Yang, P.Y., 2005. Combined removal of high-strength organics and nitrogen using two-stage entrapped mixed microbial cell (2SEMMC (R)) process. Journal of Industrial and Engineering Chemistry 11, 945-951. kitao, S.i.a.T., 1994. Wastewater treatment with microbial films. Technomic Publishing Company. Lee, N.M., Welander, T., 1996a. Reducing sludge production in aerobic wastewater treatment through manipulation of the ecosystem. Water Res. 30, 1781-1790. Lee, N.M., Welander, T., 1996b. Use of protozoa and metazoa for decerasing sludge production in aerobic wastewater treatment. Biotechnology letters 18, 429-434. Liu, Y., 2000. Effect of chemical uncoupler on the observed growth yield in batch culture of activated sludge. Water Res. 34, 2025-2030. Liu, Y., Tay, J.H., 2001. Strategy for minimization of excess sludge production from the activated sludge process. Biotechnology Advances 19, 97-107. Low, E.W., Chase, H.A., 1999a. The effect of maintenance energy requirements on biomass production during wastewater treatment. Water Res. 33, 847-853. Low, E.W., Chase, H.A., 1999b. Reducing production of excess biomass during wastewater treatment. Water Res. 33, 1119-1132. Low, E.W., Chase, H.A., Milner, M.G., Curtis, T.P., 2000. Uncoupling of metabolism to reduce biomass production in the activated sludge process. Water Res. 34, 3204-3212. Ni, B.J., Fang, F., Xie, W.M., Yu, H.Q., 2008. Growth, maintenance and product formation of autotrophs in activated sludge: Taking the nitrite-oxidizing bacteria as an example. Water Res. 42, 4261-4270. Qian, X., Yang, P.Y., Maekawa, T., 2001. Evaluation of direct removal of nitrate with entrapped mixed microbial cell technology using ethanol as the carbon source. Water Environment Research 73, 584-589. Rim, Y.-T., Yang, H.-J., Yoon, C.-H., Kim, Y.-S., Seo, J.-B., Ryu, J.-K., Shin, E.-B., 1997. A full-scale test of a biological nutrients removal system using the sequencing batch reactor activated sludge precess. Water Science and Technology 135, 241-247. Rocher, M., Goma, G., Begue, A.P., Louvel, L., Rols, J.L., 1999. Towards a reduction in excess sludge production in activated sludge processes: biomass physicochemical treatment and biodegradation. Applied Microbiology and Biotechnology 51, 883-890. Song, C.Y., Cho, E., Wang, Z., Yang, P.Y., 2006. Removal of organic and nitrogen and molecular weight distribution of residual soluble organic from entrapped mixed microbial cells and activated sludge processes. Water Environment Research 78, 2501-2507. Spinosa, L., Lotito, V., 2003. A simple method for evaluating sludge yield stress. Advances in Environmental Research 7, 655-659. Strand, S.E., Harem, G.N., Stensel, H.D., 1999. Activated-sludge yield reduction using chemical uncouplers. Water Environment Research 71, 454-458. Takdastan, A., Mehrdadi, N., Azimi, A.A., Torabian, A., Bidhendi, G.N., 2009. Investigation of intermittent chlorination system in biological excess sludge reduction by sequencing batch reactors.Iran. J. Environ. Health Sci. Eng. 6, 53-60. Tanaka, K., Tada, M., Kimata, T., Harada, S., Fujii, Y., Mizuguchi, T., Mori, N., Emori, H., 1991. Development of new nitrogen removal system using nitrifying bacteria immobilized in synthetic resin pellets. Water Science and Technology 23, 681-690. Tramper, J., Grootjen, D.R.J., 1986. Operating performance of nitrobacter-agilis immobilized in carrageenan. Enzyme and Microbial Technology 8, 477-480. Tsubone, T., Ogaki, Y., Yoshiy, Y., Takahashi, M., 1992. Effects of biomass entrapment and carrier properties on the performance of an air-fluidized-bed biofilm reactor. Water Environment Research 64, 884-889. Wang, W.H., Jung, Y.J., Kiso, Y., Yamada, T., Min, K.S., 2006. Excess sludge reduction performance of an aerobic SBR process equipped with a submerged mesh filter unit. Process Biochemistry 41, 745-751. Wei, Y.S., Liu, J.X., 2006. Sludge reduction with a novel combined worm-reactor. Hydrobiologia 564, 213-222. Wei, Y.S., Van Houten, R.T., Borger, A.R., Eikelboom, D.H., Fan, Y.B., 2003a. Comparison performances of membrane bioreactor and conventional activated sludge processes on sludge reduction induced by Oligochaete. Environ. Sci. Technol. 37, 3171-3180. Wei, Y.S., Van Houten, R.T., Borger, A.R., Eikelboom, D.H., Fan, Y.B., 2003b. Minimization of excess sludge production for biological wastewater treatment. Water Res. 37, 4453-4467. Wong, P.K., Kwok, S.C., 1992. Accumulation of nickel ion (Ni2+) by Immoblized mmoblized cells of enterorbacter species. Biotechnology letters 14, 629-634. Yang, P.Y., Cao, K., Kim, S.J., 2002. Entrapped mixed microbial cell process for combined secondary and tertiary wastewater treatment. Water Environment Research 74, 226-234. Yang, P.Y., Chen, H.J., Kim, S.J., 2003a. Integrating entrapped mixed microbial cell (EMMC) process for biological removal of carbon and nitrogen from dilute swine wastewater. Bioresource Technology 86, 245-252. Yang, P.Y., Su, R., Kim, S.J., 2003b. EMMC process for combined removal of organics, nitrogen and an odor producing substance. Journal of Environmental Management 69, 381-389. Yang, P.Y., Zhang, Z.Q., Jeong, B.G., 1997. Simultaneous removal of carbon and nitrogen using an entrapped-mixed-microbial-cell process. Water Res. 31, 2617-2625. Low, E.W., Chase, H.A., 1999. Reducing production of excess biomass during wastewater treatment. Water Res. 33, 1119-1132. Kokufuta, E., M. Shimohashi, and L. Nakamura, 1998 “Simultaneously Occurring Nitrification and Denitrification under Oxygen Gradient by Polyelectrolyte Complex Co-immobilized Nitrosomonas europaea and Paracoccus denitrificans Cells.” Biotechonl Bioeng. ,.31, 382-384. Sumino, T., H. Nakamura, N. Mori, Y. Kawaguchi and M. Tada,1992 “Immobilization of Nitrifying Bacteria in Porous Pellets of Urethane Gel for Removal of Ammonium Nitrogen from Waste-water.” Applied Microbiology Biotechnology, 36, 556-560. 林正芳、林瑤勤、羅棋穎、吳忠信,2002,「水及廢水處理理論與實務」,六合出版社。 江晃榮,2000,「生物技術與污染防制(一)固定化微生物在廢水處理上之應用」,工業汙染防治技術叢書,廢水耗氧處理論著彙編(下),台北,頁31-40。 李公哲,2000,「工業廢水處理技術(四)」,工業汙染防治技術叢書,廢水耗氧處理論著彙編(上),台北,頁55-65。 陳秋揚,2000,「工業廢水生物處理及應用」,工業汙染防治技術叢書,廢水耗氧處理論著彙編(上),台北,頁195-224。 陳國誠,吳建一,2000,「微生物固定化技術在廢水處理的應用」,工業汙染防治技術叢書,廢水耗氧處理論著彙編(下),台北,頁269-292。 陳國誠,1991,「廢水生物處理學」,台北茂昌。 陳國誠,1989,「微生物酵素工程學」,台北藝軒。 吳美惠,張芳賓,朱昱學,1996,「固定化微生物廢水處理技術評估」,工業污染防治,第59 期,頁81-110。 李國鏞,游若篍,2001,「微生物學」,華香園出版社,台北。 營建署委託研究報告,2002,社團法人台灣下水道協會「台灣地區家庭污水量及污染量推估研究」,頁27-31。 洪仁陽,2002,「污泥水解技術」,化工資訊月刊Vol.6,頁66-73。 王祖珩等編輯,2005,「廢水污泥減量技術手冊」,經濟部工業局。 陳見財,陳志銘、莊敏芳,2004,「污泥處理技術彙編」,經濟部工業局。 朱敬平,李篤中,2001,污泥處置,國立台灣大學台大工程學刊,Vol.82,頁49-76。 徐儆暉,林宜長,1995,包陷式混合微生物處理食品有機廢水之動力模式,中華衛誌,Vol.14,頁129-137。 | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/9129 | - |
| dc.description.abstract | 傳統式活性污泥法為在廢水處理中最廣泛使用的生物處理方法,其可利用微生物可效地去除水中溶解性有機物,但由於傳統式活性污泥法會產生大量之廢棄物,造成後續處理之問題。
固定化生物處理技術為一種可同時去除COD及氨氮之生物處理方法,且固定化細胞具有高機械強度與耐久性穩定性高、操作簡易等特性,但對於其污泥產率(sludge yield)仍尚未進行研究,因此本研究以固定化細胞處理技術搭配不同實驗參數(污泥粒徑、水利停留時間、曝氣模式)進行污泥產率之研究。 利用合成廢水(COD:300 mg/L,總氮:25 mg/L),配合不同粒徑之固定化細胞(1 cm及2.5 cm粒徑)、不同曝氣模式(連續曝氣、1小時曝氣/1小時不曝氣、1小時曝氣/2小時不曝氣)及水力停留時間(6小時及12小時)進行實驗,其COD去除率均可達92.3%以上;總氮去除率約介於22.9~64.8%。於污泥生長係數方面,以1 cm粒徑之污泥粒,搭配連續曝氣(10 L/min)及12小時之水力停留時間所得到之污泥產量較低,其污泥生長係數為0.107 kg SS/kg COD,其餘則介於0.11~0.275 kg SS/kg COD。 於高COD之合成廢水(COD:1000 mg/L,總氮:25 mg/L)搭配連續曝氣及12小時之水力停留時間進行連續一星期之試驗方面,其結果得知,COD平均去除率為94.6%,總氮去除率約99.6%以上;於污泥生長係數方面,1 cm之污泥粒為0.228 kg SS/kg COD,2.5 cm之污泥粒為0.270 kg SS/kg COD。 本研究另採取食品廢水 (TCOD 773 mg/L,SCOD 556 mg/L,NH3-N平均13.2 mg/L,NO3-平均1.3 mg/L) 搭配連續曝氣及12小時之水利停留時間進行連續一星期之測試,結果發現,COD之平均去除率達89.4%,總氮去除率達95.9%以上;於污泥生長係數方面,1 cm之污泥粒為0.018 kg SS/kg COD,2.5 cm之污泥粒則為0.047 kg SS/kg COD。 | zh_TW |
| dc.description.abstract | The conventional active sludge process is the most widespread used biological treatment in wastewater treatment plant, which uses microorganisms to remove the soluble organic matter effectively in water. However, the conventional active sludge process will emit a large amount of wastes and produce problems to the following treatment processes.
The Immobilized biological treatment is a technology simultaneously to remove COD and ammonia nitrogen and the immobilized cell has high density mixed microbial cells, high stability and durability, low effluent suspended solids, a short start-up period and easy to restart the operation but no studies have been focus on sludge yield of immobilized biological treatment yet. Thus, this study used immobilized cell processing technology with different experiment parameter (sludge particle size, hydraulic retention time, and aeration mode) to study the sludge yield. The lab scale immobilized biological treatment process is fed by synthesis wastewater to provide COD:300 mg/L and NH3-N:25 mg/L, with different particle size of immobilized cell (1 cm and 2.5 cm), different aeration mode (continuous aeration, 1 hour aeration/1 hour non-aeration, 1 hour aeration /2 hours non-aeration) and different hydraulic retention time (6 hours and 12 hours). The SCOD removal efficiencies can reach more than 92.3% and the total nitrogen removal efficiencies approximately is situated between the rate of 22.9~64.8%. Moreover, sludge yield is low, 0.107 kg SS/kg COD, for 1 cm particle size of immobilized biological treatment with continuous aeration (10 L/min) and 12 hour hydraulic retention time, the rest were between 0.11~0.275 kg SS/kg COD. As for the high COD concentration of synthesis wastewater (COD:1000 mg/L, NH3-N: 25 mg/L) with the continuous aeration mode and 12 hour hydraulic retention time carries continuously a week of experimental aspect, the results show that the average COD removal efficiency is 94.6% and total nitrogen removal rate is approximately above 99.6%. In addition, the sludge yield of 1 cm particle size is 0.27 kg SS/kg COD, and 2.5 cm particle size is 0.27 kg SS/kg COD. On the other hand, this research also adopts food industrial wastewater which concentrates 773 mg/L of TCOD, 556 mg/L of SCOD, 13.2 mg/L of NH3-N, 1.3 mg/L of NO3-N with the continuous aeration mode and 12 hour hydraulic retention time carries continuously a week of experiment aspects, the results show that the average COD removal efficiency is 89.4% and the total nitrogen removal rate can reach more than 95.9%. The sludge yield of 1 cm particle size is 0.018 kg SS/kg COD and 2.5 cm particle size is 0.047 kg SS/kg COD. | en |
| dc.description.provenance | Made available in DSpace on 2021-05-20T20:10:15Z (GMT). No. of bitstreams: 1 ntu-98-R96541209-1.pdf: 1026014 bytes, checksum: 7f1fdb0808c23bb102a7286b291c1f66 (MD5) Previous issue date: 2009 | en |
| dc.description.tableofcontents | 謝誌 i
中文摘要 ii ABSTRACT iii 第一章 前言 1 1-1研究目的及內容 1 第二章文獻回顧 2 2-1廢水生物處理方法 2 2-1-1懸浮生長式生物處理法 2 2-1-2固定生長式生物處理法 2 2-2生物處理之污泥產生 4 2-2-1生物處理污泥產率 6 2-2-2污泥產率減量研究 6 2-3固定化微生物 8 2-3-1固定化微生物技術 9 2-3-2固定化細胞相關研究 11 2-3-3利用固定化細胞進行廢水生物處理之優點及限制 12 第三章 材料與研究方法 15 3-1實驗內容與項目 15 3-2實驗設備 17 3-3實驗方法 19 3-3-1固定化微生物製作 19 3-4分析方法 20 3-5污泥產率計算 22 第四章 結果與討論 23 4-1合成廢水 23 4-1-1不同粒徑之污泥產生量 24 4-1-2不同水力停留時間之污泥產生量 27 4-1-3不同曝氣模式之污泥產生量 32 4-2高COD合成廢水 41 4-3 食品廢水 45 4-4家庭污水(模型廠) 49 第五章 結論與建議 53 5-1結論 53 5-2 建議 54 參考文獻 55 附錄 62 | |
| dc.language.iso | zh-TW | |
| dc.title | 固定式生物程序之污泥產率研究 | zh_TW |
| dc.title | Sludge Yield of Immobilized Biological System | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 97-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 林郁真,康佩群 | |
| dc.subject.keyword | 固定化細胞,固定化生物程序,污泥產率, | zh_TW |
| dc.subject.keyword | Immolilized cell,Immobilized Biological System,Sludge yield, | en |
| dc.relation.page | 71 | |
| dc.rights.note | 同意授權(全球公開) | |
| dc.date.accepted | 2009-07-29 | |
| dc.contributor.author-college | 工學院 | zh_TW |
| dc.contributor.author-dept | 環境工程學研究所 | zh_TW |
| 顯示於系所單位: | 環境工程學研究所 | |
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