4.7 Article

Enhancing the applicability of forward osmosis membrane process utilizing food additives as draw solutes

Journal

JOURNAL OF MEMBRANE SCIENCE
Volume 638, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.memsci.2021.119705

Keywords

Forward osmosis (FO); Pressure assisted osmosis (PAO); Whey concentration; Food additive; Draw solute; Monosodium glutamate (MSG)

Funding

  1. Korea Institute of Science and Technology [2E26251, 2E28120]
  2. Korea Environment Industry & Technology Institute (KEITI) through the Industrial Facilities & Infrastructure Research Program - Korea Ministry of Environment (MOE) [116953]
  3. Ministry of Science, ICT & Future Planning, Republic of Korea [2E26251] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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The study investigated the use of food additives as draw solutes for forward osmosis to concentrate liquid food products. While the osmotic pressures generated by food additives were similar to or higher than NaCl, the water flux produced was significantly lower due to severe internal concentration polarization. However, the reverse solute flux of food additives was low, indicating low contamination. The study also demonstrated the potential of pressure-assisted osmosis with food additive draws for dewatering whey and lactose solutions in the food industry.
Food additives as draw solutes were investigated to improve the feasibility of forward osmosis (FO) for concentration of liquid food products. Three widely used food additives were selected: monosodium glutamate (MSG), sodium saccharine, and trisodium citrate. The osmotic pressures generated by food additives were measured to be similar or even higher than that of NaCl. However, the water flux produced by FO using food additives was 70-78% lower than that of NaCl. This observation was mainly attributed to severe internal concentration polarization (ICP). Conversely, the reverse solute flux (RSF) of food additives in the FO process was low at only 3-9% of that of NaCl, suggesting they pose a low contamination. The FO process using MSG draw solutions yielded a 15% solid content of whey. To further improve FO concentration, pressure-assisted osmosis (PAO) was adopted for dewatering whey and lactose solutions. The PAO process applying a pressure of 10 bar to feed solution increased the water flux by 36% (whey) and 49% (lactose) with a 2 M MSG draw solution, thus demonstrating the potential of the developed FO/PAO with food additive draws for the food industry.

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