Hybrid PSf/TNT-SO<sub>3</sub>H Ultrafiltration Membrane Fouling by Sodium Alginate: Effect of Permeation Flux on Fouling Resistance and Desalination Efficiency

<div>DSC heating curves for membranes with different water contents at temperature range -30–+30°C.</div>

Adsorption Science & Technology

fig3

Figure 3

Figure 3: Hybrid PSf/TNT-SO<sub>3</sub>H Ultrafiltration Membrane Fouling by Sodium Alginate: Effect of Permeation Flux on Fouling Resistance and Desalination Efficiency 

Figure 3 | Hybrid PSf/TNT-SO3H Ultrafiltration Membrane Fouling by Sodium Alginate: Effect of Permeation Flux on Fouling Resistance and Desalination Efficiency 