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http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/69609完整後設資料紀錄
| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 陳發林(Falin Chen) | |
| dc.contributor.author | Tzu-Chin Lin | en |
| dc.contributor.author | 林子覲 | zh_TW |
| dc.date.accessioned | 2021-06-17T03:20:58Z | - |
| dc.date.available | 2028-12-31 | |
| dc.date.copyright | 2018-08-06 | |
| dc.date.issued | 2018 | |
| dc.date.submitted | 2018-06-22 | |
| dc.identifier.citation | 1. M. Elimelech, W.A. Phillip, The future of seawater desalination: energy, technology, and the environment, Science 333 (2011) 712–717.
2. 經濟部水利署,水庫濱水帶植物,2006. 3. 網站資訊: http://www.wri.org/resources/charts-graphs/water-stress-country 4. G.L. Meerganz von Medeazza, “Direct” and socially induced environmental impacts of desalination. Desalination, 185 (2005) 57–70. 5. 網站資訊:http://hssszn.com/archives/29533 6. Ibrahim S. Al-Mutaz, A comparative study of RO and MSF desalination plants, Desalination 106 (1996) 99–106. 7. L. Garzia-Rodriguez, Seawater desalination driven by renewable energies: a review, Desalination, 143 (2002) 103–113. 8. S. Al Kharabsheh, An innovative reverse osmosis desalination system using hydrostatic pressure, Desalination, 196 (2006) 210–214 . 9. DL. Abdella, Reverse osmosis desalination. Marine Technol 31(1994)195–200. 10. 網站資訊: https://puretecwater.com/reverse-osmosis/what-is-reverse-osmosis 11. R. Dashtpour, SN. Al-Zubaidy, Wave Powered Deep-Sea Desalination Scheme, International Conference on Environment Energy and Biotechnology 33(2012)154-162. 12. M. Reali, M. deGerloni, A. Sampaolo, Submarine and underground reverse osmosis schemes for energy-efficient seawater desalination, Desalination 109 (1997) 269–275. 13. D. Colombo, M. de Gerloni and M. Reali, An energy-efficient submarine desalination plant, Desalination, 122 (1999) 171–176. 14. P. Pacenti, M. de Gerloni, M. Reali, D. Chiaramonti, S.O. Gärtner, P. Helm and M. Stöhr, Submarine seawater reverse osmosis desalination system, Desalination, 126 (1999) 213–218. 15. C. Charcosset,C. Falcone ,M. Combe, Hydrostatic pressure plants for desalination via reverse osmosis, Renewable Energy 34(2009)2878–2882. 16. SJ Hastings, Desalination system. U.S. Patent Application No. 12/519,493. 17. G Mokhtar. Gravity force-driven desalination unit: a sustainable energy substitute of high-pressure pumps.Desalination and Water Treatment 56(2015): 2602-2611. 18. TOYOBO-HOLLOSEP-HL10255SI. http://www.toyobo-global.com/seihin/ro/spec-HL10255SI.htm. 19. 網站資訊: http://www.cdmr.cn/bbs/showthread.asp?threadid=1355 20. 網站資訊: https://www.cnyes.com/futures/basicmetal.aspx | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/69609 | - |
| dc.description.abstract | 在21世紀因為人口的快速成長、氣候的變遷等等因素,讓水資源變得非常的缺乏,為了解決世界水資源缺乏的問題,於是發展出了非常多不同的海水淡化技術,雖然海水淡化的技術可以讓人們有取之不盡,用之不竭的水資源,不過在做海水淡化的同時,會產生出Brine排放的問題,噪音汙染、空氣汙染還有巨大的能量消耗等等嚴重的問題。
為了改善在做海水淡化時,巨大的能量消耗,本論文將有設計一和設計二的海水淡化廠,設計一海水淡化廠是利用海深600公尺所產生出來的靜水壓去推動RO過濾膜,而產生出純水,在產量為12540(m3/day),每一噸純水所需要的能量消耗為2.11(KWh/m3),在產量為20000(m3/day)時,每一噸純水所需要的能量消耗為2.018 (KWh/m3),與傳統的海水淡化廠3-10(KWh/m3),明顯少了許多。 在設計二的海水淡化廠中,利用了靜水壓和帕斯卡的原理來做海水淡化,在十六級凹槽的海水淡化廠,每一噸純水所需要的能量消耗為3.17(KWh/m3),雖然所需要的能量消耗與傳統海水淡化廠的最低能量消耗差不多,不過在現在真實有在運作的海水淡化廠每一噸純水所需要的能量消耗在3(KWh/m3)左右的,還是佔了整體的少數,而且凹槽式海水淡化廠不需要像設計一有600公尺深的豎井,可這樣以使整體的施工成本更低且更讓整個海水淡化廠更好維修。 | zh_TW |
| dc.description.abstract | In the 21st century, due to the rapid population growth and climate change, water resources have become extremely scarce. In order to solve the problem of the lack of water resources in the world, we have developed many different seawater desalination technologies.
The desalination technology allows people to have inexhaustible water resources, but at the same time you desalinate seawater, it will cause Brine emission problems, noise pollution, air pollution, and huge energy consumption. In order to reduce the huge energy consumption during seawater desalination, this paper includes two designs of desalination plant to solve this problem. The first desalination plant applies static hydrostatic pressure which generated by 600 meters deep to push the RO membrane to produce pure water. When the water production rate is 12540 (KWh / m3), the energy consumption per ton of pure water is 2.018 (KWh/m3), and then we increase the production rate to 20,000 (m3/day) , the energy consumption per ton of pure water is 2.11 (KWh/m3).This result is obviously lower than the traditional desalination plant 3-10 (KWh/m3). In the second deisign, we apply hydrostatic pressure and pascal's principle for seawater desalination. In the desalination plant with sixteen grooves, the energy consumption per ton of pure water is 3.17 (KWh/m3). Although the required energy consumption is almost the same as the lowest energy consumption of the conventional desalination plant,for many desalination plants, 3 (KWh/m3)per ton of pure water is still a minority. In addition, the grooved desalination plant does not need to design a shaft with a depth of 600 meters, which can make the overall construction cost lower and make the entire desalination plant more maintainable. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-17T03:20:58Z (GMT). No. of bitstreams: 1 ntu-107-R05543070-1.pdf: 2619426 bytes, checksum: 5e93478ffe56fd86c501136bb60bff9c (MD5) Previous issue date: 2018 | en |
| dc.description.tableofcontents | 誌 謝 i
摘要 ii Abstract iii 目錄 iv 圖目錄 vi 表目錄 viii 第一章 緒論 1 1.1 研究背景 1 1.1.1 RO過濾膜運作原理 2 1.2 研究動機 4 1.3 研究方法 5 第二章 現有技術文獻回顧 6 2.1 傳統海水淡化廠 6 2.1.1水淡化廠的運作原理 6 2.1.2海水淡化廠適用地形與能量的消耗 8 2.2 高效能潛艇式海水淡化廠 8 2.2.1海水淡化廠的運作原理 8 2.2.2海水淡化廠適用地形與能量的消耗 9 2.3 高效能地底式海水淡化廠 10 2.3.1海水淡化廠的運作原理 10 2.3.2海水淡化廠適用地形與能量的消耗 11 2.4 潛艇式海水RO海水淡化系統 12 2.4.1海水淡化廠的運作原理 12 2.4.2海水淡化廠適用地形與能量的消耗 13 2.5 波浪能深海海水淡化廠 14 2.5.1海水淡化廠的運作原理 14 2.5.2海水淡化廠適用地形與能量的消耗 16 2.6 靜水壓RO海水淡化廠 16 2.6.1海水淡化廠的運作原理 16 2.6.2海水淡化廠適用地形與能量的消耗 18 2.7 海水淡化廠(By Hastings & Hills) 18 2.7.1海水淡化廠的運作原理 19 2.8 創新靜水壓海水淡化系統 20 2.8.1海水淡化廠的運作原理 20 2.8.2海水淡化廠適用地形與能量的消耗 22 2.9 重力驅動海水淡化原件 22 2.9.1海水淡化廠的運作原理 23 2.9.2海水淡化廠適用地形與能量的消耗 24 2.10 總結 24 第三章 設計一 26 3.1 設計一海水淡化廠作用原理 26 3.2 能量消耗分析 28 3.2.1設計一能量的消耗(產量為12540(m3/day)) 30 3.2.1設計一能量的消耗(產量為20000(m3/day)) 33 第四章 設計二 36 4.1設計描述與原理 36 4.2設計二海水淡化廠基本計算 38 4.2.1海水淡化廠運作步驟和原理 42 4.2.3海水淡化廠耗能計算 47 4.3結果 54 第五章 結論與未來展望 56 5.1結論 56 5.2未來展望 57 參考文獻 58 | |
| dc.language.iso | zh-TW | |
| dc.subject | 能量消耗 | zh_TW |
| dc.subject | 逆滲透 | zh_TW |
| dc.subject | 帕斯卡原理 | zh_TW |
| dc.subject | 靜水壓 | zh_TW |
| dc.subject | 海水淡化 | zh_TW |
| dc.subject | desalination | en |
| dc.subject | hydrostatic pressure | en |
| dc.subject | pascal principle | en |
| dc.subject | reverse osmosis | en |
| dc.subject | energy consumed | en |
| dc.title | 凹槽式低耗能海水淡化廠設計與分析 | zh_TW |
| dc.title | Design and calculation of Groove-type low energy consumed desalination plant | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 106-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 鍾志昂(Chih-Ang Chung),張敏興(Min-Hsing Chang) | |
| dc.subject.keyword | 海水淡化,靜水壓,帕斯卡原理,逆滲透,能量消耗, | zh_TW |
| dc.subject.keyword | desalination,hydrostatic pressure,pascal principle,reverse osmosis,energy consumed, | en |
| dc.relation.page | 59 | |
| dc.identifier.doi | 10.6342/NTU201800941 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2018-06-25 | |
| dc.contributor.author-college | 工學院 | zh_TW |
| dc.contributor.author-dept | 應用力學研究所 | zh_TW |
| 顯示於系所單位: | 應用力學研究所 | |
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