A study of the osmotic membrane bioreactor process using a sodium chloride solution and an industrial effluent as draw solutions

被引:23
作者
Lujan-Facundo, M. J. [1 ]
Soler-Cabezas, J. L. [1 ]
Mendoza-Roca, J. A. [1 ]
Vincent-Vela, M. C. [1 ]
Bes-Pia, A. [1 ]
Donate-Hernandez, S. [2 ]
机构
[1] Univ Politecn Valencia, Inst Seguridad Ind Radiofis & Medioambiental, Camino Vera S-N, E-46022 Valencia, Spain
[2] DAM, Ave Benjamin Franklin 21,46980 Parque Tecnol, Valencia, Spain
关键词
Forward osmosis; Osmotic membrane bioreactor; Membrane fouling; Wastewater treatment; Draw solution; MUNICIPAL WASTE-WATER; OSMOSIS MEMBRANE; RETENTION TIME; BIOLOGICAL TREATMENT; PHOSPHORUS RECOVERY; PERFORMANCE; MICROFILTRATION; HYBRID; TECHNOLOGY; MITIGATION;
D O I
10.1016/j.cej.2017.04.062
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Osmotic membrane bioreactor (OMBR) is an emerging membrane process which has gained interest in the recent years because of the low energy consumption and the high effluent quality. The osmotic membrane bioreactor combines a forward osmosis (FO) membrane and a biological treatment. However, salt reverse flux is the main problem because of the negative effect of the salt concentration increase in the reactor on the microbial activity. This is the reason why the study of a suitable draw solution (DS) is very important in the overall performance of the reactor. This study compares the process performance using two draw solutions: a 53 g L-1 NaCI solution and a real waste water solution (waste water from an absorption column consisting mainly of SO42- and NH4-N with concentrations of 153 g L-1 and 19 g L-1, respectively). The comparison is focused on the salt reverse flux during the reactor operation, the mixed liquor characteristics, the membrane fouling and the overall performance. The results indicated that the industrial wastewater showed a higher salt reverse flux, but also a less severe fouling and a higher the osmotic pressure difference in comparison with the NaCl solution. In terms of chemical oxygen demand (COD) removal efficiencies, both draw solutions attained values higher than 80%, though the efficiency was slightly lower when the industrial effluent was used as DS. This was related to the higher conductivity reached in the bioreactor when the industrial effluent was used as draw solution. In spite of it, the use of this industrial effluent as draw solution is strongly recommended because of the high permeate fluxes yielded, the low membrane fouling and the lack of necessity of regenerating the draw solution. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:603 / 610
页数:8
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