Scale-up of osmotic membrane bioreactors by modeling salt accumulation and draw solution dilution using hollow-fiber membrane characteristics and operation conditions

被引:42
作者
Kim, Suhan [1 ]
机构
[1] Pukyong Natl Univ, Dept Civil Engn, Pusan 608739, South Korea
基金
新加坡国家研究基金会;
关键词
Osmotic membrane bioreactor; Scale-up; Modeling; Salt accumulation; Draw solution dilution; CONCENTRATION POLARIZATION; FLUX BEHAVIOR; OSMOSIS MEMBRANES; PERFORMANCE; FO;
D O I
10.1016/j.biortech.2014.03.101
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A full-scale osmotic membrane bioreactor (OMBR) model was developed to simulate salt accumulation, draw solution (DS) dilution, and water flux over the hollow-fiber membrane length. The model uses the OMBR design parameters, DS properties, and forward osmosis (FO) membrane characteristics obtained from lab-scale tests. The modeling results revealed a tremendous water flux decline (10 > 0.82 LMH) and short solids retention time (SRT: 5 days) due to salt accumulation and DS dilution when OMBR is scaled up using commercially available DS and FO membrane. Simulated water flux is a result of interplay among reverse salt flux, internal and external concentration polarization (ICP and ECP). ECP adversely impacts water flux considerably in full-scale OMBR although it is often ignored in previous works. The OMBR model makes it possible to select better DS properties (higher flow rate and salt concentration) and FO membranes with higher water flux propensity in full-scale operation. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:88 / 95
页数:8
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