Forward osmosis for concentration of anaerobic digester centrate

被引:472
作者
Holloway, Ryan W.
Childress, Amy E.
Dennett, Keith E.
Cath, Tzahi Y.
机构
[1] Colorado Sch Mines, Div Environm Sci & Engn, Golden, CO 80401 USA
[2] Univ Nevada, Dept Civil & Environm Engn, Reno, NV 89557 USA
[3] Tahoe Truckee Sanitat Agcy, Truckee, CA 96161 USA
关键词
forward osmosis; reverse osmosis; wastewater treatment; biosolids; anaerobic digestion; centrate;
D O I
10.1016/j.watres.2007.05.054
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The nutrient-rich liquid stream produced during the dewatering of digested biomass (i.e., the centrate) is commonly mixed with the influent raw wastewater at wastewater treatment facilities. This increases the nitrogen and phosphorus loading on biological processes, increases operating costs, and in some cases, results in increased nutrient concentrations in the final effluent. Forward osmosis (FO) is a membrane treatment process that was investigated at bench scale to determine its feasibility to concentrate centrate under both batch and continuous operating conditions. The continuous bench-scale system used FO as pretreatment for reverse osmosis (RO). Results demonstrated that high water flux and high nutrient rejection could be achieved. The combined FO/RO process exhibited sustainable flux over an extended time period. A mathematical model was developed in order to determine the specific energy, power, and membrane area requirements for a larger-scale centrate treatment process. Modeling results indicated that to optimize power and membrane area requirements, the system should be operated at approximately 70% water recovery. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4005 / 4014
页数:10
相关论文
共 19 条
[1]  
Anderson D.K., 1977, CONCENTRATION DILUTE
[2]  
[Anonymous], 1999, FULL SCALE EXPERIENC
[3]  
BEAUDRY EG, 1997, DIRECT OSMOSIS CONCE, P1
[4]   Removal of natural steroid hormones from wastewater using membrane contactor processes [J].
Cartinella, Joshua L. ;
Cath, Tzahi Y. ;
Flynn, Michael T. ;
Miller, Glenn C. ;
Hunter, Kenneth W., Jr. ;
Childress, Amy E. .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2006, 40 (23) :7381-7386
[5]   Membrane contactor processes for wastewater reclamation in space Part I. Direct osmotic concentration as pretreatment for reverse osmosis [J].
Cath, TY ;
Gormly, S ;
Beaudry, EG ;
Flynn, MT ;
Adams, VD ;
Childress, AE .
JOURNAL OF MEMBRANE SCIENCE, 2005, 257 (1-2) :85-98
[6]   Membrane contactor processes for wastewater reclamation in space II. Combined direct osmosis, osmotic distillation, and membrane distillation for treatment of metabolic wastewater [J].
Cath, TY ;
Adams, D ;
Childress, AE .
JOURNAL OF MEMBRANE SCIENCE, 2005, 257 (1-2) :111-119
[7]   Forward osmosis: Principles, applications, and recent developments [J].
Cath, Tzahi Y. ;
Childress, Amy E. ;
Elimelech, Menachem .
JOURNAL OF MEMBRANE SCIENCE, 2006, 281 (1-2) :70-87
[8]  
FRANSON MAH, 1998, STANDARD MATHODS EXA
[9]   Biological treatment of ammonium-rich wastewater by partial nitritation and subsequent anaerobic ammonium oxidation (anammox) in a pilot plant [J].
Fux, C ;
Boehler, M ;
Huber, P ;
Brunner, I ;
Siegrist, H .
JOURNAL OF BIOTECHNOLOGY, 2002, 99 (03) :295-306
[10]   Relating organic fouling of reverse osmosis membranes to intermolecular adhesion forces [J].
Lee, S ;
Elimelech, M .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2006, 40 (03) :980-987