Tetrabutylphosphonium trifluoroacetate ([P4444]CF3 COO) thermoresponsive ionic liquid as a draw solution for forward osmosis process = Larutan ionik responsif haba tetrabutilfosfonium trifluoroasetat ([P4444]CF3 COO) sebagai larutan penarik untuk proses osmosis kehadapan

Forward osmosis (FO) is recognized as a potential membrane technology that utilizes low energy for water desalination. It is driven by natural osmotic pressure difference between feed solution and draw solution across semipermeable membrane. Pure water will permeate from the salinity feed water to t...

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Bibliographic Details
Main Authors: Nyan, Phang Sook, Syed Mohd Saufi, Tuan Chik, Syamsul Bahari, Abdullah, Mazrul Nizam, Abu Seman, Malyanah, Mohd Taib
Format: Article
Language:English
Published: Malaysian Society of Analytical Sciences 2018
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Online Access:http://umpir.ump.edu.my/id/eprint/33506/1/Tetrabutylphosphonium%20trifluoroacetate%20%28%5BP4444%5DCF3%20COO%29%20thermoresponsive%20ionic%20liquid.pdf
http://umpir.ump.edu.my/id/eprint/33506/
https://doi.org/10.17576/mjas-2018-2204-05
https://doi.org/10.17576/mjas-2018-2204-05
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Summary:Forward osmosis (FO) is recognized as a potential membrane technology that utilizes low energy for water desalination. It is driven by natural osmotic pressure difference between feed solution and draw solution across semipermeable membrane. Pure water will permeate from the salinity feed water to the draw solution side. In order to produce pure water, it is necessary to find the best draw solute that exhibits high draw ability and can separate the permeated water efficiently from the draw solution. In the current study, lower critical solution temperature (LCST) thermoresponsive ionic liquid (IL) of tetrabutylphosphonium trifluoroacetate ([P4444]CF3COO) was synthesized as the draw solute for FO process. ([P4444]CF3COO) is dissolved in water below its critical temperature of 29°C and becomes two layered above this critical temperature. [P4444]CF3COO IL showed high water flux of 0.44 ± 0.007 LMH compared to the water flux of 0.32 ± 0.049 LMH for the NaCl draw solute at the same draw solution concentration. Applying thermoresponsive IL as the draw solute in FO process has the potential to treat high salinity of feed stream with ease of water recovery and draw solute regeneration.