Modelling and Prediction of Permeate Flux in the Ultrafiltration Recovery of Sodium Lignosulfonate from Aqueous Solution

Modelling and data fitting for the prediction of permeate flux during ultrafiltration (UF) of a model feed solution of sodium lignosulfonate was carried out following resistance in series, gel polarization and Kedem Katchalsky equations. The experiments were conducted in a laboratory UF unit equipped with PES/HFUF asymmetric membrane under specific operating conditions by altering some parameters including solute concentration, transmembrane pressure (TMP), and cross flow velocity (CFV). The maximum experimental permeate flux was observed at TMP of 3.92 bar and CFV 0.527 ms-1 was 19.6 × 10-6 m3m-2s-1. The theoretical and experimental volumetric flux was plotted, and their extent of resemblance was compared and validated statistically. The study sheds light on the effective upcycling of sodium lignosulfonate from spent liquor via ultrafiltration.

Authors

Institutions

Publication Details

Journal
Acta chimica slovenica
Published
2025-09-18
DOI
https://doi.org/10.17344/acsi.2025.9163
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Modelling and Prediction of Permeate Flux in the Ultrafiltration Recovery of Sodium Lignosulfonate from Aqueous Solution

Haresh K. Dave, Vinay Patel, Kaushik Nath, Tejal M. Patel
Acta chimica slovenica
Membrane Separation Technologies
article

Modelling and Prediction of Permeate Flux in the Ultrafiltration Recovery of Sodium Lignosulfonate from Aqueous Solution

Haresh K. Dave, Vinay Patel, Kaushik Nath, Tejal M. Patel
article en

Abstract

Modelling and data fitting for the prediction of permeate flux during ultrafiltration (UF) of a model feed solution of sodium lignosulfonate was carried out following resistance in series, gel polarization and Kedem Katchalsky equations. The experiments were conducted in a laboratory UF unit equipped with PES/HFUF asymmetric membrane under specific operating conditions by altering some parameters including solute concentration, transmembrane pressure (TMP), and cross flow velocity (CFV). The maximum experimental permeate flux was observed at TMP of 3.92 bar and CFV 0.527 ms-1 was 19.6 × 10-6 m3m-2s-1. The theoretical and experimental volumetric flux was plotted, and their extent of resemblance was compared and validated statistically. The study sheds light on the effective upcycling of sodium lignosulfonate from spent liquor via ultrafiltration.

Acta chimica slovenicaVol. 72(3)
University of Fort Hare (ZA), Gujarat Technological University (IN), Viña del Mar University (CL), Cytel (United States) (US)
Openalex Percentile: Top 76%
Membrane Separation Technologies
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.