Effects of step-feeding and internal recycling on nitrogen removal in ceramic membrane bioreactors, and their hydraulic backwashing characteristics

被引:13
作者
Chung, Jaeshik [1 ,2 ]
Kim, Gyobeom [1 ]
Seo, Kyu Won [1 ,3 ]
Jin, Jaejin [1 ,4 ]
Choi, Yong Su [1 ]
机构
[1] Korea Inst Sci & Technol, Ctr Water Resource Cycle Res, Seoul 136791, South Korea
[2] Univ Florida, Dept Environm Engn Sci, Gainesville, FL 32611 USA
[3] Korea Univ, Grad Sch, Dept Biotechnol, Seoul 136701, South Korea
[4] Univ Seoul, Dept Environm Engn, Seoul, South Korea
关键词
Ceramic membrane; CMBR; Hydraulic bacicwashing; Internal recycling; Step-feeding; WASTE-WATER TREATMENT; NUTRIENT REMOVAL; PERFORMANCE; PHOSPHORUS;
D O I
10.1016/j.seppur.2014.10.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Both lab-scale (50 L/day) and pilot-scale (10 m(3)/day) ceramic membrane bioreactors (CMBRs), equipped with two additional implements (step-feeding and internal recycling), have been tested for the removal of nitrogen and organic matter from municipal wastewater. During the 180 days of operation, 0.5Q of step-feeding increased the removal rate of total nitrogen by 46.2% in the lab-scale CMBR, whereas a 59.0% increase was observed with the additional 3Q internal recycling in the pilot-scale CMBR. This was presumably due to the supply of insufficient carbon source as an electron donor in the denitrification stage. The ceramic membrane also exhibited high rigidity sufficient for periodic bacicwashing using the highly-pressurized permeate. A constant flux test with 30 s of backwashing after every 9.5 min of filtration successfully removed foulants from the pores of the ceramic membrane, and instantaneously restored the trans-membrane pressure (TMP). During the test, the TMP in case of without the hydraulic backwashing steadily increased (20-80 kPa) for 40 min, whereas it took more than two times to reach the same TMP in the case of with the hydraulic backwashing, which eventually doubled the time span between required chemical washings. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:219 / 226
页数:8
相关论文
共 35 条
[11]   Performance deterioration and structural changes of a ceramic membrane bioreactor due to inorganic abrasion [J].
Cicek, N ;
Dionysiou, D ;
Suidan, MT ;
Ginestet, P ;
Audic, JM .
JOURNAL OF MEMBRANE SCIENCE, 1999, 163 (01) :19-28
[12]   PREPARATION AND CHARACTERIZATION OF A COMPOSITE PALLADIUM-CERAMIC MEMBRANE [J].
COLLINS, JP ;
WAY, JD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (12) :3006-3013
[13]  
de Silva DGV, 1998, WATER SCI TECHNOL, V38, P505, DOI 10.1016/S0273-1223(98)00551-4
[14]   Ceramic membrane as a pretreatment for reverse osmosis: interaction between marine organic matter and metal oxides [J].
Dramas, Laure ;
Croue, Jean-Philippe .
DESALINATION AND WATER TREATMENT, 2013, 51 (7-9) :1781-1789
[15]   VOLATILE FATTY-ACIDS AS ORGANIC-CARBON SOURCES IN DENITRIFICATION [J].
FASS, S ;
GANAYE, V ;
URBAIN, V ;
MANEM, J ;
BLOCK, JC .
ENVIRONMENTAL TECHNOLOGY, 1994, 15 (05) :459-467
[16]   CRITICAL FLUX CONCEPT FOR MICROFILTRATION FOULING [J].
FIELD, RW ;
WU, D ;
HOWELL, JA ;
GUPTA, BB .
JOURNAL OF MEMBRANE SCIENCE, 1995, 100 (03) :259-272
[17]   Enhanced nutrient removal in a modified step feed process treating municipal wastewater with different inflow distribution ratios and nutrient ratios [J].
Ge, Shijian ;
Peng, Yongzhen ;
Wang, Shuying ;
Guo, Jianhua ;
Ma, Bin ;
Zhang, Liang ;
Cao, Xu .
BIORESOURCE TECHNOLOGY, 2010, 101 (23) :9012-9019
[18]   ANALYTICAL STUDY OF LEAD ION-SELECTIVE CERAMIC MEMBRANE ELECTRODE [J].
HIRATA, H ;
HIGASHIYAMA, K .
BULLETIN OF THE CHEMICAL SOCIETY OF JAPAN, 1971, 44 (09) :2420-+
[19]   Comparison of fouling characteristics in different pore-sized submerged ceramic membrane bioreactors [J].
Jin, Le ;
Ong, Say Leong ;
Ng, How Yong .
WATER RESEARCH, 2010, 44 (20) :5907-5918
[20]   Fouling behaviour, regeneration options and on-line control of biomass-based power plant effluents using microporous ceramic membranes [J].
Kumar, S. Mahesh ;
Madhu, G. M. ;
Roy, Sukumar .
SEPARATION AND PURIFICATION TECHNOLOGY, 2007, 57 (01) :25-36