傳統的活性污泥法(ASP)再加上利用膜生物反應器(MBR)分離的技術，能使含剝離液廢水經生物處理單元後直接產生高品質的出流水。在實場運轉研究中，已經成功的說明MBR技術的優勢，與(P. Glueckstern et al, 2008)在以色列實場運轉流程相同，(Jian-Jun et al, 2006)在新加坡新生水NEWater回收流程也是採用MBR-RO的回收處理技術。
本研究目的要探討出一個最佳的回收水處理系統選擇技術，對已運轉5年的A公司ASP-MBR-RO系統與B公司的生物床接觸曝氣法(Biopolisher)-砂濾塔(MMF)-逆滲透(RO)系統比較。2家公司的水回收率如何經過長期運轉改善經驗穩定維持回收率75%以上。另一目的驗證含剝離液廢水回收水再利用處理系統的最佳性能數據及操作參數，以達到最低的運轉操作成本。
在B公司的Bio-polisher-MMF-RO技術，運轉成本約只有8.29 元/m3，主要是採用只需1小時水力停留時間的生物處理系統Bio-polisher，並對高單價的生物生長營養劑進行減量及本土化測試運轉，成功降低運轉成本的藥劑費83 %，每噸廢水的藥劑費由8.8元/m3下降至1.46元/m3。而A公司的ASP-MBR-RO技術，運轉成本約在17.85 元/m3，兩者相差約9.5元/m3。主因是廢水組成不同，A公司處理含剝離液廢水需採用水力停留時間48小時的生物處理單元，及過濾單元採用新技術的MBR，以致運轉費用較高。
最佳化的回收再利用處理系統為Bio-polisher+MBR+ACF+RO，以A公司為例，當原物料採用生物易分解剝離液(N300)，並選用MBR膜可直接從生物單元生產出高品質的收水(<0.1 NTU)、高TOC去除率<90%及水回收率>75%。最佳化運轉成本由17.85元/m3下降至8.82元/m3，佔地面積由800下降至600 m2(減少25%)，年回收水量1,247,935 m3/y，約可供應台南市生活用水2.6天。

The conventional activated sludge process (ASP) plus the use of membrane bioreactor (MBR) separation technology which enables the stripping liquid containing waste water biological treatment unit directly out of high-quality water. In the real field operation studies, has successfully explained the advantages of MBR technology, P. Glueckstern et al (2008), in the field of operation of the process the same as the real Israel, Jian-Jun et al (2006), NEWater recovery process in Singapore also use MBR-RO's recycling technology.Best of recycling processing system Bio-polisher + MBR + ACF + RO, can produce directly out from a biological unit high-quality collection of water (<0.1 NTU), high TOC removal <90% and water recovery> 75%. Best of operating costs decreased from 17.85 NT/m3 to 8.82 NT/m3, and can supply about 2.6 days Tainan living water.

1. Ashraf Al Ashhab, Herzberg Moshe, and Gillor Osnat. "Biofouling of reverse-osmosis membranes during tertiary wastewater desalination : Microbial community composition" water research 50, 2014.
2. Lai Berlin and K Wen Shieh "Batch monoethylamine degradation via nitrate respiration. " Water Research 30(10):2530-2534, 1996.
3. Bont De, J. A. M., J. P. van Dijiken, and W. Harder "Dimethyl sulfoxide and dimethyl sulfide as a carbon, sulfur and energy source for growth of Hyphomicrobium S. " Journal of general microbiology 127:315-323, 1981.
4. Carlsson, H., H. Aspegren and A. Hilmer. " Interactions Between Wastewater Quality and Phosphorus Release in the Anaerobic Reactor of the EBPR Process. " Wat. Res., Vol. 30, No. 6, pp. 1517-1527, 1996.
5. Dreizin Y., A. Tenne , and D. Hoffman. "Integrating large scale seawater desalination plants within Israel’s water supply system." Received 10 January 2007, 2007.
6. Glueckstern, P. , M. Priel, E. Gelman, and N. Perlov. "Wastewater desalination in Israel" Desalination 222 151–164, 2008.
7. Qin Jian-Jun, Kekre Kiran Arun, Tao Guihe, Oo Maung Htun, Wai Maung Nyunt, Lee Ting Cui, Viswanath Bala, and Seah Harry. "New option of MBR-RO process for production of NEWater from domestic sewage" Journal of Membrane Science 272 ,70–77, 2006.
8. Chew Michele Y.C. , Watanabe Chihiro , and Tou Yuji "The challenges in Singapore NEWater development: Co-evolutionary development for innovation and industry evolution" Technology in Society 33, 2011.
9. Chew Michele Y.C. , Watanabe Chihiro, and Tou Yuji "The challenges in Singapore NEWater development: Co-evolutionary" Technology in Society 33, 2011.
10. Newman Stephen A. "Acid and sour gas treating processes. " Houston TX, Gulf Publishing Co, 1985.
11. Osmonics, G. "The Filtration Spectrum. " Minnesota, USA, GE Osmonics, 1996.
12. Park Se-Jin, Yoon Tai-Il, Bae Jae-Ho, Seo Hyung-Joon, and Hyo-Jung Park. " Biological treatment of wastewater containing dimethyl sulphoxide from the semi-conductor industry " Process Biochemistry 36：579-589, 2001.
13. Vincent Lenouvel, and Lafforgue Michel. "Chevauche Catherine, and Rhetore Pauline. The enerey cost of water independence：the case of Singapore" Water Science & Technology 70.5, 2014.
14. Wang Ying , Gitis Vitaly, Lee Jintae , and Herzberg Moshe. "Effects of shear rate on biofouling of reverse osmosis membrane during tertiary wastewater desalination" Journal of Membrane Science 427, 2013.
15. Zinder,S. H. and T. D. Brock. “Dimethyl sulphoxide reduction by micro-organisms.” Journal of general microbiology 105:342-55, 1978.
16. 王根樹 "以活性碳吸附水中背景有機物之研究"，行政院國家科學委員會專題研究計畫成果報告, 2001.
17. 李曉芬 "高科技產業園區廢水除磷技術操作成本比較分析" 碩士論文, 朝陽科技大學環境工程與管理系, 2008.
18. 林宏霖 "探討生物分解光電產業製程廢水之反應動力特性研究" 碩士論文,國立成功大學環境工程研究所, 2006.
19. 陳廷光、倪振鴻、陳重男 "生物薄膜與逆滲透程序應用於TFT-LCD製程廢水處理與再利用" 工業污染防治 第89期, 2004.
20. 馮育澤 " TFT-LCD製程廢水回收系統薄膜阻塞問題研究" 碩士論文, 國立成功大學環境工程研究所, 2012.
21. 黃淑君 "不織布薄膜反應槽好氧生物分解TFT-LCD製程有機廢水程序功能及生態變化之研究" 碩士論文, 國立成功大學環境工程研究所, 2006.
22. 廖威智 "薄膜電晶體液晶顯示器(TFT-LCD)製程有機廢水處理與回收再利用之研究" 碩士論文, 國立交通大學環境工程研究所, 2003.