陈梅雪1,
杨敏1,2,
郁达伟1,2,
郑嘉熹1,2,
魏源送1,
冀春苗3,
王晓爽3,
常江3
1.中国科学院生态环境研究中心,北京100085
2.中国科学院大学,北京 100049
3.北京排水集团科技研发中心,北京 100022
基金项目: 国家水体污染控制与治理科技重大专项(2015ZX07203-005)
国家自然科学基金资助项目(21777161,3,21777161)
国家重点研发计划(2016YFE0118500)
Design and operation optimization on full-scale membrane bioreactor using CFD
LIU Mengmeng1,2,,CHEN Meixue1,
YANG Min1,2,
YU Dawei1,2,
ZHENG Jiaxi1,2,
WEI Yuansong1,
JI Chunmiao3,
WANG Xiaoshuang3,
CHANG Jiang3
1.Research Center for Eco-Environment Science, Chinese Academy of Sciences, Beijing 100085, China
2.University of Chinese Academy of Sciences, Beijing 100049, China
3.Center of Technology Development, Beijing Drainage Group Co.Ltd., Beijing 100022, China
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摘要:基于计算流体力学(CFD)方法,使用Eulerian多相流模型,对500 m3·d-1的膜生物反应器中曝气管布置方式以及4种气水比(10∶1、15∶1、20∶1和25∶1)进行优化研究,通过对不同反应器构型内部流场、速度场和膜面液体流速进行分析比较,同时借助停留时间分布(RTD)实验对模拟结果进行实验验证。结果表明:曝气管“对齐”布置方式优于“间隔”和“垂直”布置;考虑膜面冲刷以及能耗方面,确定最佳气水比为20∶1,此时反应器内形成了循环流动,膜面冲刷效果比较好,低速区占比较小,对降低膜污染有很好的作用。
关键词: 膜生物反应器/
计算流体力学/
流场模拟/
优化曝气/
膜污染
Abstract:Based on the computational fluid dynamics method, the Eulerian multiphase flow model was used to simulate the 500 m3·d-1 aerobic MBR and optimize its arrangement of aerators and four gas-water ratios (10∶1,15∶1,0∶1,5∶1). The internal flow field, velocity field and membrane velocity of different reactor configurations were analyzed and compared, and the simulation results were verified by means of residence time distribution (RTD).The results show that the “alignment” arrangement of the aeration pipe is better than that of “interval” and “vertical”. Considering the membrane surface erosion and energy consumption, the optimum gas-water ratio is 20∶1. In this operation status, the reactor flow, membrane erosion effect is better, and low-speed area accounted for relatively small, which has a good effect to reduce membrane pollution.
Key words:membrane bioreactor (MBR)/
computational fluid dynamics (CFD)/
flow field simulation/
optimization of aeration/
membrane fouling.
[1] | JUDD S.The MBR Book:Principles and Applications of Membrane Bioreactors for Water and Wastewater Treatmen[M].北京:科学出版社,2012 |
[2] | 王琦,樊耀波.膜生物反应器在污水处理与回用中的能耗分析[J].膜科学与技术,2012,2(3):95-103 |
[3] | LE-CLECH P, CHEN V, FANE T A G.Fouling in membrane bioreactors used in wastewater treatment[J].Journal of Membrane Science,2006,4(1):17-53 |
[4] | CHANG I S, CLECH P L, JEFFERSON B, et al.Membrane fouling in membrane bioreactors for wastewater treatment[J].Journal of Environmental Engineering,2002,8(11):1018-1029 |
[5] | DREWS A.Membrane fouling in membrane bioreactors:Characterisation, contradictions, cause and cures[J].Journal of Membrane Science,2010,3(1/2):1-28 |
[6] | AL-HALBOUNI D, TRABER J, LYKO S, et al.Correlation of EPS content in activated sludge at different sludge retention times with membrane fouling phenomena[J].Water Research,2008,2(6/7):1475-1488 |
[7] | CHARFI A,BEN A N,HARMAND J.Analysis of fouling mechanisms in anaerobic membrane bioreactors[J].Water Research,2012,6(8):2637-2650 |
[8] | KRAUME M,WEDI D,SCHALLER J,et al.Fouling in MBR:What use are lab investigations for full scale operation?[J].Desalination, 2009,6(1/2/3):94-103 |
[9] | NDINISA N,FANE A,WILEY D,et al.Fouling control in a submerged flat sheet membrane system.Part II:Two-phase flow characterization and CFD simulations[J].Separation Science and Technology,2006,1(7):1411-1445 |
[10] | 王福军.计算流体动力学分析:CFD软件原理与应用[M].北京:清华大学出版社, 2004 |
[11] | 贾晓强.气液固三相生物反应器流动与降酚特性动态行为研究[D].天津:天津大学, 2008 |
[12] | 杨敏,徐荣乐,袁星,等.膜生物反应器ASM-CFD 耦合仿真研究进展[J].膜科学与技术,2015,5(6):126-133 |
[13] | YANG M,WEI Y,ZHENG X,et al.CFD simulation and optimization of membrane scouring and nitrogen removal for an airlift external circulation membrane bioreactor[J].Bioresource Technology,2016,9:566-575 |
[14] | YANG M,YU D,LIU M,et al.Optimization of MBR hydrodynamics for cake layer fouling control through CFD simulation and RSM design[J].Bioresource Technology,2016,7:102-111 |
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[16] | 张宇,吴志超,藏莉莉,等.CFD在平板膜MBR设计及运行优化中的研究[J].环境工程学报, 2016,0(2):735-741 |
[17] | 张晴,樊耀波,徐荣乐.气升循环分体式MBR中H循环管水力学研究[J].膜科学与技术,2014,4(1):39-44 |
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基于CFD的大型膜生物反应器的设计及运行优化
柳蒙蒙1,2,,陈梅雪1,
杨敏1,2,
郁达伟1,2,
郑嘉熹1,2,
魏源送1,
冀春苗3,
王晓爽3,
常江3
1.中国科学院生态环境研究中心,北京100085
2.中国科学院大学,北京 100049
3.北京排水集团科技研发中心,北京 100022
基金项目: 国家水体污染控制与治理科技重大专项(2015ZX07203-005) 国家自然科学基金资助项目(21777161,3,21777161) 国家重点研发计划(2016YFE0118500)
关键词: 膜生物反应器/
计算流体力学/
流场模拟/
优化曝气/
膜污染
摘要:基于计算流体力学(CFD)方法,使用Eulerian多相流模型,对500 m3·d-1的膜生物反应器中曝气管布置方式以及4种气水比(10∶1、15∶1、20∶1和25∶1)进行优化研究,通过对不同反应器构型内部流场、速度场和膜面液体流速进行分析比较,同时借助停留时间分布(RTD)实验对模拟结果进行实验验证。结果表明:曝气管“对齐”布置方式优于“间隔”和“垂直”布置;考虑膜面冲刷以及能耗方面,确定最佳气水比为20∶1,此时反应器内形成了循环流动,膜面冲刷效果比较好,低速区占比较小,对降低膜污染有很好的作用。
English Abstract
Design and operation optimization on full-scale membrane bioreactor using CFD
LIU Mengmeng1,2,,CHEN Meixue1,
YANG Min1,2,
YU Dawei1,2,
ZHENG Jiaxi1,2,
WEI Yuansong1,
JI Chunmiao3,
WANG Xiaoshuang3,
CHANG Jiang3
1.Research Center for Eco-Environment Science, Chinese Academy of Sciences, Beijing 100085, China
2.University of Chinese Academy of Sciences, Beijing 100049, China
3.Center of Technology Development, Beijing Drainage Group Co.Ltd., Beijing 100022, China
Keywords: membrane bioreactor (MBR)/
computational fluid dynamics (CFD)/
flow field simulation/
optimization of aeration/
membrane fouling
Abstract:Based on the computational fluid dynamics method, the Eulerian multiphase flow model was used to simulate the 500 m3·d-1 aerobic MBR and optimize its arrangement of aerators and four gas-water ratios (10∶1,15∶1,0∶1,5∶1). The internal flow field, velocity field and membrane velocity of different reactor configurations were analyzed and compared, and the simulation results were verified by means of residence time distribution (RTD).The results show that the “alignment” arrangement of the aeration pipe is better than that of “interval” and “vertical”. Considering the membrane surface erosion and energy consumption, the optimum gas-water ratio is 20∶1. In this operation status, the reactor flow, membrane erosion effect is better, and low-speed area accounted for relatively small, which has a good effect to reduce membrane pollution.