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Cleaning Efficiency of Biodegradable Products on Fouled Ceramic Membranes by Analogue Produced Water
Figure 2: Fouling Evolution for Membrane Pore Sizes
Figure 3: Cleaning by Flushing Fouled Membrane
0.30
0.50
0.45
0.25
0.40
0.20
0.35
0.30
0.15
0.25
0.10
0.1µm
Flux recovery 0.20
T
ransmembrane pressure (bar)
0.2µm
0.05
0.5µm 0.15
0.10
0.00
020406080 100 120
0.05
Operation time (minutes)
0.00
0.1µm 0.2µm 0.5µm
the analogue PW can potentially penetrate the membrane with the larger
Membrane pore size
pore size of 0.5µm and cause pore plugging/blocking, whereas for the
membrane with a pore size of 0.1µm, the solid particles mainly create a The efficiency of the alkaline and acid solutions vary as a function of
layer on the membrane surface. Furthermore, the foulant deposited on membrane pore sizes. The alkaline solution Derquim+ has a higher
the surface is not strongly bound to the membrane surface and thus flux recovery than Ultrasil 115 (92, 90and 68% versus 82, 74 and
cleaning by inducing high shear forces during flushing is helpful. 59% for 0.1, 0.2 and 0.5µm, respectively), and the acid solution
SurfactronCD50 has a higher flux recovery than Ultrasil 73 for all
The effectiveness of a single cleaning step for alkaline and acid membrane pore sizes (82, 85 and 68% versus 85, 80 and 49% for
solutions was investigated. The cleaning agent removes the foulant by 0.1, 0.2 and 0.5µm, respectively). Although the pH of Ultrasil 115 is
displacing foulants from the membrane surface due to their strong higher than that of Derquim+, the surfactant mixture in Derquim+ is
surface adsorption, emulsifying oils and solubilising hydrophobic more efficient since it has a stronger solubilisation effect on the oil on
foulants by incorporating them into surfactant micelles.
10
the membrane surface. The pH of Ultrasil 73 is lower than that of
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