膜生物反应器污水再生工程的运行与优化
收稿日期: 2005-09-15
修回日期: 2005-09-15
网络出版日期: 2010-10-01
Operation and optimization of membrane bioreactor (MBR) for the wastewater regeneration engineering
Received date: 2005-09-15
Revised date: 2005-09-15
Online published: 2010-10-01
郭春禹, 杜启云, 王庆生 . 膜生物反应器污水再生工程的运行与优化[J]. 工业水处理, 2006 , 26(1) : 63 -66 . DOI: 10.11894/1005-829x.2006年.26（01）.63
The domestically produced PVDF hollow fiber microfilter membrane is used in combination with the submerged membrane bioreactor, which consists ofhydrolysis acidification-aerobic biochemical processes, for treating the domestic sewage in a holiday village. Its designed scale is 500 m 3 /d. The treated water is used to beautify environments. The basic technical process, equipment and structual design parameters are explained briefly. The engineering debugging and try-out operation are introduced emphatically. The running parameters are optimized through the sensitivity analysis of the water cost.
[1] 雷乐成. 污水回用新技术及工程设计
[M]. 北京: 化学工业出版 社, 2002: 38-50.
[2] 国家环保总局科技标准司.城市污水处理及污染防治技术指南
[M]. 北京: 中国环境科学出版社, 2001: 15-35.
[3] Thompson D. Immersed Membrane Bioreactors for Water Reuse: Summary of 5 Years Experience
[C]. Proceedings of 25th Annual Hawaii Water Environment Association Conference, Honolulu, Hawaii. 2003: 29-31.
[4] Lawrence Peter. Ensuring water re-use projects succeed-Institu-tional and technical issues for treated wastewater re-use[J]. desal-ination, 2003, 152(1-3): 291-298.
[5] Zhang Shaoyuan. Sewage treatment by a lowenergy membrane biore-actor[J]. Bioresource Technology, 2003, 90(2): 185-192.
[6] 郑祥, 刘俊新. 膜生物反应器的技术经济分析[J]. 给水排水, 2000, 28(3): 105-108.
[7] 刘伊生. 工程造价管理基础理论相关法规
[M]. 北京: 中国计划出 版社, 2004: 105-113.
[8] Chua H. Controlling fouling in membrane bioreactors operated with a variable throughput[J]. Desalination, 2002, 149(9): 225-229.
[9] Cornel P. Investigation of oxygen transfer rates in full scale mem-brane bioreactors[J]. Water Science and Technology, 2003, 47 (11) : 313-319.
[10] Hong S P. Fouling control in activated sludge submerged hollow fiber membrane bioreactors[J]. Desalination, 2002, 143(3):219-228.
[11] Ujang Z. The effect of aeration and non-aeration time on simultane-ous organic, nitrogen and phosphorus removal using an intermittent aeration membrane bioreactor[J]. Water Science and Technology, 2002, 46(9): 193-200.
[12] Gnirss R. Cost effective and advanced phosphorus removal in membrane bioreactors for a decentralised wastewater technology [J]. Water Science and Technology, 2003, 47(12) : 133-139.
/
| 〈 |
|
〉 |
津公网安备 12010602120337号