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  1. NTU Theses and Dissertations Repository
  2. 生物資源暨農學院
  3. 生物環境系統工程學系
請用此 Handle URI 來引用此文件: http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/31812
完整後設資料紀錄
DC 欄位值語言
dc.contributor.advisor侯文祥
dc.contributor.authorHsiao-Chuan Yehen
dc.contributor.author葉曉娟zh_TW
dc.date.accessioned2021-06-13T03:20:56Z-
dc.date.available2006-08-09
dc.date.copyright2006-08-09
dc.date.issued2006
dc.date.submitted2006-07-27
dc.identifier.citation1. A standard for the measurement of oxygen transfer in clean water. 1984. ASCE Transfer Standards Committee, New York, N.Y.
2. APHA. 1980 Standard Methods for the examination of water and wastewater. American Public Health Association, New York. p 360-361.
3. Boyd, C. E. and Watten. B. J., 1989. Aeration systems in aquaculture. CRC Critical Reviews in Aquatic Sciences 1:425-472.
4. Calabrese. R.V., Chang .T.P.K., Dang. P.T., 1986, Drop breakup in turbulent stirred-tank contactors. Part I: Effect of dispersed-phase viscosity, AIChE Journal. 32:657–666.
5. Chisti. M. Y. and Moo-Young. M. 1987, Airlift reactors Characteristics; applications and design considerations, Chem. Eng. Commun., 60, 195-242.
6. Colt. J., K. Orwicz and Bouck. G., 1991, Water quality considerations and criteria for high-density fish culture with supplemental oxygen. American Fisheries Society Symposium, 10, 372-385.
7. Cramer.1 PH.M.R. Beenackers. A.A.C.M., L.L. van Dierendonck, 1992, Hydrodynamics and mass transfer characteristics of a loop-venturi reactor with a downflow liquid jet ejector.,Chemical Engineering Journal, Sci. 47 (13/14), 3557-3564.
8. Cramer.2 PH.M.R. Van Dierendonck. L.L., Beenackers. A.A.C.M., 1992, Influence of the gas density on the gas entrainment rate and gas holdup in loop-venturi reactors, Chemical Engineering Journal, Sci. 47 (9-11), 2251-2256.
9. Cramer. P.H.M.R. Beenackers. A.A.C.M., 2001, Influence of the ejector configuration, scale and the gas density on the mass transfer characteristics of gas-liquid ejectors, Chemical Engineering Journal, 82(3):131-141.
10. Dirix. C.A.M.C., van der Wiele. K., 1990, Mass transfer in jet loop reactors, Chemical Engineering of Journal, Sci., 45 (8): 2333-2340.
11. Lage. .P.L.C. and Espo’sito. R.O., 1999, Experimental determination of bubble size distributions in bubble columns: prediction of mean bubble diameter and gas hold up, Powder Technology, 101:142-150.
12. Lawson. T., 1995. Fundamentals of Aquacultural Engineering. Chapman and Hall, New York.
13. Michael J. Moore and Claude E. Boyd, 1992, Design of small paddle wheel aerators. Aquacultural Engineering, 11:55-69.
14. Stenstrom M. K. and Gilbert. R.G, 1981, Effects of alpha, beta, and theta factor upon the design, specification and operation of aeration systems. Water Research, 15: 643-654.
15. 上野洋一郎、秦宗顯譯,2000,循環水工程的關鍵技術,水產出版社。
16. 侯文祥、譚義績,2005,微細氣泡增氧設施對淡水養殖池節水效益之研究,經濟部水利署委辦計畫成果報告,國立台灣大學水工試驗所。
17. 喻新、侯文祥,1988,兩種養殖池表面打氣設施效率之比較,未發表。
18. 蔡宗霖,2003,簡易微細氣泡產生裝置開發與應用在淡水及海水中曝氣與傳輸臭氧之研究,台灣大學生物環境系統工程研究所碩士論文,45-47頁。
19. 譚義績、侯文祥,2005,桃園農田水利會灌區蓄水池水質監測及改善示範計劃,桃園農田水利會委辦計劃成果報告,國際灌溉排水協會中華民國國家委員會,p9-13。
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/31812-
dc.description.abstract溶氧在自然水體中為水質優劣的重要指標,簡易式微細氣泡產生裝置由市售硬質塑膠管材及抽水馬達組裝而成,利用柏努利(Bernoulli)定理,改變管內水流速度,進而將空氣導入水中,產生直徑小於600μm的微細氣泡,提升水體溶氧量以改善水質環境。
本研究先分析1/8馬力至1馬力四種動力規格,共76種模組之簡易式微細氣泡裝置的增氧效果,以測量氣泡直徑,判斷系統之曝氣能力。其次,探討裝置之增氧效率、影響範圍等水質改善能力,以明確量化裝置適用範圍與操作規範;並與市面上常見之增氧設備做經濟性比較,完成多規格的微細氣泡產生裝置之基本資料建立。
依裝置標準化試驗結果,標準氧氣轉換效率以1hp動力的效果最佳,在淡水中為14.3 kgO2/hr,在海水中為63.1 kgO2/hr,明顯得知利用在海水中之曝氣效果優於淡水,而總體氧氣質傳係數及吸氣量與動力成正比,標準曝氣效率及氣泡粒徑則與動力成反比。至於本裝置應用於深水域之效果較淡水域顯著,增氧擴散範圍與水深成正比,於5公尺深水域之增氧擴散範圍可達半徑30公尺。
zh_TW
dc.description.abstractDissolved oxygen quantity serves as an indicator deterring the water quality stand or fall in water field. Simplified Microbubble Generated Device was assembled by a pump and PVC tubes, adopting Bernoulli's equation, accelerating the water velocity in the pipe to transfer air into the water. The microbubbles produced by this derive were smaller than 600 um in diameter, increasing dissolved oxygen in water to improve the water quality.
This research analyzed 4 degrees of power supply and 76 models of simplified microbubble generated devices. By measuring the diameters of microbubbles, we estimated the dispersive ability of each combination. Secondly, oxygen increasing efficiency and range were recorded as well for identifying applicable conditions and clarifying operation methods. Finally, with the comparison of other oxygen-increasing equipments, the basic data of different Simplified microbubble generated device was established.
According to the results of the experiments, the standard oxygen transfer rate (SOTR) with 1hp power supply reached its top performance. The SOTR was 14.3 kg02/hr in freshwater better that 63.1 kg02/hr in sea water.
The Overall oxygen transfer coefficient and the air inhalation were in direct ratio with power supply; the standard aerated efficiency and the diameters of bubbles were in inverse ratio with power supply. The devices showed outstanding effect in deep water since the oxygen diffused area expanded as the depth incrusted. The experiments showed that the oxygen diffused area can access to 30 meter in radius when the device was placed at 5 meter underwater
en
dc.description.provenanceMade available in DSpace on 2021-06-13T03:20:56Z (GMT). No. of bitstreams: 1
ntu-95-R93622026-1.pdf: 2502086 bytes, checksum: 6c6110b9a0cf8c80b9952b82f97f0839 (MD5)
Previous issue date: 2006
en
dc.description.tableofcontents第一章 前言…………………………………………………………1
1.1 研究緣起……………………………………………………1
1.2 研究內容與目標……………………………………………1
第二章 文獻回顧……………………………………………………3
2.1 微細氣泡產生裝置設計與原理……………………………3
2.2 溶氧相關理論………………………………………………3
2.3 曝氣理論……………………………………………………6
2.3.1 氣體佔有率……………………………………………6
2.3.2 總體氧氣質傳係數……………………………………7
2.3.3 溶氧傳遞效率相關係數………………………………9
2.3.4 氣泡粒徑………………………………………………10
2.4 曝氣設備介紹………………………………………………12
2.4.1 曝氣形式簡介…………………………………………12
2.4.2 各式噴射曝氣系統……………………………………15

第三章 材料與方法…………………………………………………18
3.1 裝置之規格化研發…………………………………………19
3.1.1 微細氣泡管規格設計用材料…………………………19
3.1.2 微細氣泡管規格化試驗方法…………………………22
3.2 裝置之增氧效率標準試驗…………………………………23
3.2.1 增氧效率試驗材料與儀器……………………………23
3.2.2 增氧效率標準試驗方法…………………………………26
3.3 微細氣泡裝置增氧裝置之應用研究………………………28
3.3.1 應用於露天蓄水池養殖水域…………………………28
3.3.2 應用於露天高密度養殖魚池水域………………………30
3.3.3 應用於自來水用小型湖庫水域………………………32
3.4 裝置經濟性分析方法………………………………………33
第四章 結果與討論…………………………………………………36
4.1 裝置規格化之結果與討論…………………………………36
4.2 裝置增氧效率試驗之結果與討論……………………………39
4.3 裝置增氧之應用結果與討論……………………………42
4.3.1 應用於露天蓄水池養殖水域…………………………42
4.3.2 應用於露天高密度養殖魚池水域………………………44
4.3.3 應用於自來水用小型湖庫水域…………………………49
4.4 裝置經濟性分析……………………………………………52
第五章 結論與建議…………………………………………………57
5.1 結論…………………………………………………………57
5.2 建議…………………………………………………………59
第六章 參考文獻…………………………………………………62
附錄A、裝置規格化試驗資料-微細氣泡放大影像…………………65
附錄B、增氧試驗計算記錄…………………………………………74
dc.language.isozh-TW
dc.subject微細氣泡zh_TW
dc.subject溶氧zh_TW
dc.subject噴射曝氣zh_TW
dc.subjectDissolved oxygenen
dc.subjectjet aeratoren
dc.subjectMicrobubbleen
dc.title簡易式微細氣泡產生裝置規格化研發與應用研究zh_TW
dc.titleThe standardization and the application research of the Simple Microbubble Generated Deviceen
dc.typeThesis
dc.date.schoolyear94-2
dc.description.degree碩士
dc.contributor.oralexamcommittee徐崇仁,喻新,謝正義
dc.subject.keyword微細氣泡,噴射曝氣,溶氧,zh_TW
dc.subject.keywordMicrobubble,jet aerator,Dissolved oxygen,en
dc.relation.page83
dc.rights.note有償授權
dc.date.accepted2006-07-30
dc.contributor.author-college生物資源暨農學院zh_TW
dc.contributor.author-dept生物環境系統工程學研究所zh_TW
顯示於系所單位:生物環境系統工程學系

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