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Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal
Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal
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Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal
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Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal
Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal

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Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal
Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal
Journal Article

Characterization and performance evaluation of in-house ultrafiltration membrane coupled with photocatalysis for 17 α -methyltestosterone hormone removal

2024
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Overview
17α-methyltestosterone (MT) hormone is a synthetic androgenic steroid hormone utilized to induce Nile tilapia transitioning for enhanced production yield. This study specifically focuses on the removal of MT through the utilization of photocatalytic membrane reactor (PMR), which employs an in-house polyvinylidene fluoride (PVDF) ultrafiltration membrane modified with 1% nanomaterials (either TiO2 or α-Fe2O3). The molecular weight cut-off (MWCO) of the in-house membrane falls within the ultrafiltration range. Under UV95W radiation, the PMR with PVDF/TiO2 and PVDF/α-Fe2O3 membranes achieved 100% MT removal at 140 and 160 min, respectively. The MT removal by the commercial NF03 membrane was only at 50%. In contrast, without light irradiation, the MT removal by all the membranes remained unchanged after 180 min, exhibiting lower performance. The incorporation of TiO2 and α-Fe2O3 enhanced water flux and MT removal of the membrane. Notably, the catalytic activity was limited by the distribution and concentration of the catalyst at the membrane surface. The water contact angle did not correlate with the water flux for the composited membrane. The degradation of MT aligned well with Pseudo-first-order kinetic models. Thus, the in-house ultrafiltration PMR demonstrated superior removal efficiency and lower operational costs than the commercial nanofiltration membrane, attributable to its photocatalytic activities.