4.8 Article

Integrated forward osmosis-membrane distillation process for human urine treatment

Journal

WATER RESEARCH
Volume 91, Issue -, Pages 45-54

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.watres.2015.12.045

Keywords

Forward osmosis; Membrane distillation; Urine treatment; Integrated system; Water regeneration

Funding

  1. National High Technology Research Program (863 Program)
  2. National Key Technology Support Program of China [2012BAC05B02]
  3. National Ministry of Education Program of China [SS2012AA062902]

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This study demonstrated a forward osmosis-membrane distillation (FO-MD) hybrid system for real human urine treatment. A series of NaCI solutions at different concentrations were adopted for draw solutions in FO process, which were also the feed solutions of MD process. To establish a stable and continuous integrated FO-MD system, individual FO process with different NaCI concentrations and individual direct contact membrane distillation (DCMD) process with different feed temperatures were firstly investigated separately. Four stable equilibrium conditions were obtained from matching the water transfer rates of individual FO and MD processes. It was found that the integrated system is stable and sustainable when the water transfer rate of FO subsystem is equal to that of MD subsystem. The rejections to main contaminants in human urine were also investigated. Although individual FO process had relatively high rejection to Total Organic Carbon (TOC), Total Nitrogen (TN) and Ammonium Nitrogen (NHt-N) in human urine, these contaminants could also accumulate in draw solution after long term performance. The MD process provided an effective rejection to contaminants in draw solution after FO process and the integrated system revealed nearly complete rejection to TOC, TN and NH4+-N. This work provided a potential treatment process for human urine in some fields such as water regeneration in space station and water or nutrient recovery from source-separated urine. (C) 2016 Elsevier Ltd. All rights reserved.

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