Effect of Nanofiltration Operating Parameters on Phytochemical Separation Using Polybenzimidazole Mixed Matrix Membrane via Organic Solvent Nanofiltration

Nanofiltration (NF) offers a sustainable, low-temperature strategy for the recovery of thermolabile bioactive compounds from plant-derived matrices; however, the coupled effects of operating parameters during NF of ethanol-rich food extracts remain insufficiently explored. This study investigated the combined influence of temperature (from 20 to 30 °C) and transmembrane pressure (TMP, 10–30 bar) on flavonoid rejection, total antioxidant activity (TAA) rejection, and permeate flux during the NF of a 75% (v/v) ethanolic citrus peel extract using a phosphoric acid-crosslinked polybenzimidazole (PBI) mixed matrix membrane. A face-centered central composite design within a response surface methodology framework produced statistically robust quadratic models ( R 2 > 0.92). Results revealed that TMP predominantly enhances rejection through increased convective transport, and interfacial accumulation, while temperature exhibited a nonlinear effect governed primarily by a reduction in hydraulic resistance, accompanied by modest increases in solute diffusivity and temperature-dependent changes in phytochemical intermolecular interactions. The observed deviation between flavonoid and TAA rejection trends reflects compositional heterogeneity and size-dependent transport of structurally diverse antioxidant species. Multi-response optimization identified an optimum at 25.3 °C and 30 bar, achieving 91.5% flavonoid rejection, 77% TAA retention and a permeate flux of 11.4 L m −2 h −1 . Fouling analysis revealed intermediate pore blocking, coupled with concentration polarization, as the dominant fouling mechanism. Under the optimized operating conditions, the optimized PBI-O membrane exhibited superior antifouling performance and cleanability, achieving a lower fouling index (FI, 40.2% vs 76.5%) and a higher flux recovery ratio (FRR, 90.5% vs 85.1%) compared with the unmodified PBI membrane. These findings provide mechanistic insight for designing sustainable NF processes for valorizing citrus waste into functional food ingredients from complex ethanolic feeds.

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Journal
Food and Bioprocess Technology
Published
2026-07-23
DOI
https://doi.org/10.1007/s11947-026-04491-y
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
0.00

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article

Effect of Nanofiltration Operating Parameters on Phytochemical Separation Using Polybenzimidazole Mixed Matrix Membrane via Organic Solvent Nanofiltration

Madhubhashitha Herath, Jayantha Epaarachchi‎, G.S.M.D.P. Sethunga, Imesha R. Samarathunga
Food and Bioprocess Technology
Membrane Separation Technologies
article

Effect of Nanofiltration Operating Parameters on Phytochemical Separation Using Polybenzimidazole Mixed Matrix Membrane via Organic Solvent Nanofiltration

Madhubhashitha Herath, Jayantha Epaarachchi‎, G.S.M.D.P. Sethunga, Imesha R. Samarathunga
article en

Abstract

Nanofiltration (NF) offers a sustainable, low-temperature strategy for the recovery of thermolabile bioactive compounds from plant-derived matrices; however, the coupled effects of operating parameters during NF of ethanol-rich food extracts remain insufficiently explored. This study investigated the combined influence of temperature (from 20 to 30 °C) and transmembrane pressure (TMP, 10–30 bar) on flavonoid rejection, total antioxidant activity (TAA) rejection, and permeate flux during the NF of a 75% (v/v) ethanolic citrus peel extract using a phosphoric acid-crosslinked polybenzimidazole (PBI) mixed matrix membrane. A face-centered central composite design within a response surface methodology framework produced statistically robust quadratic models ( R 2 > 0.92). Results revealed that TMP predominantly enhances rejection through increased convective transport, and interfacial accumulation, while temperature exhibited a nonlinear effect governed primarily by a reduction in hydraulic resistance, accompanied by modest increases in solute diffusivity and temperature-dependent changes in phytochemical intermolecular interactions. The observed deviation between flavonoid and TAA rejection trends reflects compositional heterogeneity and size-dependent transport of structurally diverse antioxidant species. Multi-response optimization identified an optimum at 25.3 °C and 30 bar, achieving 91.5% flavonoid rejection, 77% TAA retention and a permeate flux of 11.4 L m −2 h −1 . Fouling analysis revealed intermediate pore blocking, coupled with concentration polarization, as the dominant fouling mechanism. Under the optimized operating conditions, the optimized PBI-O membrane exhibited superior antifouling performance and cleanability, achieving a lower fouling index (FI, 40.2% vs 76.5%) and a higher flux recovery ratio (FRR, 90.5% vs 85.1%) compared with the unmodified PBI membrane. These findings provide mechanistic insight for designing sustainable NF processes for valorizing citrus waste into functional food ingredients from complex ethanolic feeds.

Food and Bioprocess TechnologyVol. 19(8)
University of Southern Queensland (AU), University of Moratuwa (LK)
University of Southern Queensland
Responsible consumption and production
Openalex Percentile: Top 17%
Membrane Separation Technologies
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