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Optimizing the aeration condition for membrane bioreactor based on the characteristics of transmerbrane pressure increasing rate
Authors: YING Jingqiang,GAO Yanchang,YANG Yongzhe
Units: School of Environmental and Municipal Engineering,Xi’an University of Architecture and Technology,Xi’an 710055,China
KeyWords: Membrane bioreactor; transmembrane pressure; aeration intensities; process control
ClassificationCode:X703.1;TQ028.8
year,volume(issue):pagination: 2014,34(2):45-50

Abstract:
 Submerged membrane bioreactor (MBR) was employed for petrochemical industry wastewater treatment. Transmerbrane pressure (TMP) and the TMP increasing rate (K) have been investigated under different aeration rates (300L/h, 150L/h and 75L/h). The result indicated that the evolution of TMP followed a simple exponential relationship with filtration time, i.e.  . K varied from 0 to 2.5 Pa/s under different aeration conditions. Change of aeration intensities presented insignificantly impact on the rising tendency of the K value. However, the aeration rates can change the characteristics of K increasing rate. The higher aeration rate can result in the slower increase of K. The result indicated that K could be potentially used to optimize the aeration in MBR and thus reducing the membrane fouling of MBR.

Funds:
高等学校博士学科点专项科研基金(20116120110008);陕西省自然科学基础研究计划重点项目(2010JZ008)

AuthorIntro:
应京强(1989-),男,浙江温州人,硕士生,从事膜生物反应器研究 *通讯联系人

Reference:
[1]Fenu A,Roels J,Wambecq T,et al. Energy audit of a full scale MBR system[J].Desalination,2010,262:121-128.
[2]Krzeminski P,Jaap H J M van der Graaf,Jules B van Lier. Specific energy consumption of membrane bioreactor (MBR) for sewage treatment[J]. Water science and Technology,2012,65(2):380-392.
[3]Delgado S,Villarroel R,González E. Effect of the shear intensity on fouling in submerged membrane bioreactor for wastewater treatment[J]. Journal of membrane science,2008,311:173-181.
[4]Ueda T,Hata K,Kikuoka Y,et al. Effect of aeration on suction pressure in a submerged membrane bioreactor[J]. Water Research,1997,31(3):489-494.
[5]Huyskens C,Brauns E,Hoof E V,et al. Validation of a supervisory control system for energy savings in membrane bioreactors[J]. Water Research,2011,45:1443-1453.
[6] Ferrero G,Monclús H,Buttiglieri G,et al. Development of a control algorithm for air-scour reduction in membrane bioreactors for wastewater treatment[J]. Journal of chemical technology and biotechnology,2011,86:784-789.
[7] Ferrero G,Monclús H,Buttiglieri G,et al. Automatic control system for energy optimization in membrane bioreactors[J]. Desalination,2010,268:276-280.
[8]Ginzburg B F,Yacoub F,Cote P L,et al. Process control for an immersed membrane system[P].United States,A1,0042312,2011/2/24.
[9]Monclús H,Ferrero G,Buttiglieri G,et al. Online monitoring of membrane fouling in submerged MBRs[J]. Desalination,2011,277:414-419.
[10]Huyskens C,Brauns E,Hoof E V,et al. A new method for the evaluation of the reversible and irreversible fouling propensity of MBR mixed liquor[J]. Journal of membrane science,2008,323:185-192.
[11]Geng Z,Hall E R,Bérubé P R. Membrane fouling mechanisms of a membrane enhanced biological phosphorus removal process[J]. Journal of membrane science,2007,296:93-101.
[12]Howell J A,Chua H C,Arnot T C. In situ manipulation of critical flux in a submerged membrane bioreactor using variable aeration rates,and effects of membrane history[J].Journal of membrane science,2004,242:13-19.
 

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