A rotary spacer system for energy-efficient membrane fouling control in oil/water emulsion filtration

• Main Authors: Mat Nawi, Normi Izati, Mohd. Lazis, Afiq, Aulia Rahma, Aulia Rahma, Muthia Elma, Muthia Elma, Bilad, Muhammad Roil, Md. Nordin, Nik Abdul Hadi, Wirzal, Mohd. Dzul Hakim, Shamsuddin, Norazanita, Suhaimi, Hazwani, Yusof, Norhaniza
• Format: Article
• Language: English
• Published: MDPI 2022
• Subjects: Q Science (General)
• Online Access: http://eprints.utm.my/103219/1/NorhanizaYusof2022_ARotarySpacerSystemforEnergy.pdf; http://eprints.utm.my/103219/; http://dx.doi.org/10.3390/membranes12060554

Membrane fouling deteriorates membrane filtration performances. Hence, mitigating membrane fouling is the key factor in sustaining the membrane process, particularly when treating fouling-prone feed, such as oil/water emulsions. The use of spacers has been expanded in the membrane module system, including for membrane fouling control. This study proposed a rotating spacer system to ameliorate membrane fouling issues when treating an oil/water emulsion. The system’s effectiveness was assessed by investigating the effect of rotating speed and membrane-to-disk gap on the hydraulic performance and the energy input and through computational fluid dynamics (CFD) simulation. The results showed that the newly developed rotary spacer system was effective and energy-efficient for fouling control. The CFD simulation results proved that the spacer rotations induced secondary flow near the membrane surface and imposed shear rate and lift force to exert fouling control. Increasing the rotation speed to an average linear velocity of 0.44 m/s increased the permeability from 126.8 ± 2.1 to 175.5 ± 2.7 Lm−2h−1bar−1 . The system showed better performance at a lower spacer-to-membrane gap, in which increasing the gap from 0.5 to 2.0 cm lowered the permeability from 175.5 ± 2.7 to 126.7 ± 2.0 Lm−2h−1bar−1 . Interestingly, the rotary system showed a low energy input of 1.08 to 4.08 × 10−3 kWhm−3 permeate when run at linear velocities of 0.27 to 0.44 ms−1 . Overall, the findings suggest the competitiveness of the rotary spacer system as a method for membrane fouling control.