Holloway Ryan W, Childress Amy E, Dennett Keith E, Cath Tzahi Y
Tahoe-Truckee Sanitation Agency, 13720 Joerger Drive, Truckee, CA 96161, USA.
Water Res. 2007 Sep;41(17):4005-14. doi: 10.1016/j.watres.2007.05.054. Epub 2007 Jun 3.
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.
消化生物质脱水过程中产生的富含营养物的液流(即离心液)通常在污水处理设施中与进水原废水混合。这增加了生物处理过程中的氮和磷负荷,提高了运营成本,在某些情况下,还导致最终出水的营养物浓度增加。正向渗透(FO)是一种膜处理工艺,在实验室规模上进行了研究,以确定其在间歇和连续运行条件下浓缩离心液的可行性。连续实验室规模系统使用FO作为反渗透(RO)的预处理。结果表明,可以实现高水通量和高营养物截留率。FO/RO组合工艺在较长时间内表现出可持续的通量。开发了一个数学模型,以确定更大规模离心液处理工艺的特定能量、功率和膜面积要求。建模结果表明,为了优化功率和膜面积要求,系统应在约70%的水回收率下运行。