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Fouling characterization in entrapped cells-based-membrane bioreactor treating wastewater
被引:17
|作者:
Juntawang, Chaipon
[1
]
Rongsayamanont, Chaiwat
[2
]
Khan, Eakalak
[3
]
机构:
[1] North Dakota State Univ, Environm & Conservat Sci Program, Fargo, ND 58108 USA
[2] Prince Songkla Univ, Fac Environm Management, Hat Yai 90112, Thailand
[3] North Dakota State Univ, Dept Civil & Environm Engn, CIE Bldg,Room 201,Dept 2470,POB 6050, Fargo, ND 58108 USA
关键词:
Bound extracellular polymeric substances (bEPS);
Entrapped cell;
Fouling;
Membrane bioreactor;
Soluble microbial products (SMP);
SOLUBLE MICROBIAL PRODUCTS;
SLUDGE CHARACTERISTICS;
MBR SYSTEMS;
CARRIERS;
REACTOR;
EPS;
IMMOBILIZATION;
PERFORMANCE;
FILTRATION;
REDUCTION;
D O I:
10.1016/j.seppur.2016.11.045
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Membrane fouling in an entrapped cells-based-membrane bioreactor (E-MBR) treating synthetic medium strength municipal wastewater was investigated. Laboratory scale models of E-MBR and regular (suspended cell) membrane bioreactor (S-MBR) were operated in parallel. The two systems showed comparable performances on organic matter and nutrient removal. The removal efficiencies of soluble chemical oxygen demand and ammonia of E-MBR were 95.6 +/- 0.9% and 92.6 +/- 2.1% while those of S-MBR were 95.8 +/- 0.8% and 93.3 +/- 0.8%. Membrane fouling was monitored based on transmembrane pressure through a constant permeate flux at 10.63 L/m(2).h. Due to lower concentrations of bound extracellular polymeric substances (bEPS) and soluble microbial products (SMP), E-MBR experienced less fouling and provided longer operation time before required chemical cleaning compared to S-MBR (16 days for E-MBR and 9 days for S-MBR). bEPS in E-MBR consisted of higher molecular weight compounds and had a broader molecular weight distribution than those in S-MBR. The Fourier transform infrared analysis of bEPS suggested proteins and carbohydrates as major components. According to the 3 dimension fluorescence excitation-emission matrix spectra, SMP in E-MBR were mainly tryptophan,, protein-like and humic acid-like substances, while those in S-MBR were mainly humic acid-like substances, hydrophobic acid substances and fulvic acid substances. The particles size of sludge in E-MBR was smaller than that in S-MBR. The delayed membrane fouling in E-MBR is a great advantage as it lowers costs associated with membrane cleaning processes and prolongs the membrane lifespan. (C) 2016 Elsevier B.V. All rights reserved.
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页码:321 / 329
页数:9
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