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• W1968553657 abstract "Abstract We evaluated the performance of trimethylamine–carbon dioxide (TMA–CO 2 ) as a potential thermolytic draw solution for engineered osmosis. Water flux and reverse solute flux with TMA–CO 2 draw solution were measured in forward osmosis (FO) and pressure retarded osmosis (PRO) modes using thin-film composite (TFC) and cellulose triacetate (CTA) FO membranes. Water flux with the TMA–CO 2 draw solution was comparable to that obtained with the more common ammonia–carbon dioxide (NH 3 –CO 2 ) thermolytic draw solution at similar (1 M) concentration. Using a TFC–FO membrane, the water fluxes produced by 1 M TMA–CO 2 and NH 3 –CO 2 draw solutions with a DI water feed were, respectively, 33.4 and 35.6 L m −2  h −1 in PRO mode and 14.5 and 15.2 L m −2  h −1 in FO mode. Reverse draw permeation of TMA–CO 2 was relatively low compared to NH 3 –CO 2 , ranging from 0.1 to 0.2 mol m −2  h −1 in all experiments, due to the larger molecular size of TMA. Thermal separation and recovery efficiency for TMA–CO 2 was compared to NH 3 –CO 2 by modeling low-temperature vacuum distillation utilizing low-grade heat sources. We also discuss possible challenges in the use TMA–CO 2 , including potential adverse impact on human health and environments." @default.
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• W1968553657 date "2015-01-01" @default.
• W1968553657 modified "2023-10-17" @default.
• W1968553657 title "Performance evaluation of trimethylamine–carbon dioxide thermolytic draw solution for engineered osmosis" @default.
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• W1968553657 doi "https://doi.org/10.1016/j.memsci.2014.09.026" @default.
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