PVDF/CaCO3 composite hollow fiber membrane for CO2 absorption in gas-liquid membrane contactor

Porous hydrophobic polyvinylidene fluoride (PVDF) composite hollow fiber membranes were fabricated via phase inversion method by embedding different amounts of hydrophobic calcium carbonate (CaCO3) nano-particles in the polymer matrix. The effects of nano-particle loadings on the morphology, structu...

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Main Authors: Kofal, M. Fosi, Mustafa, A., Ismail, Ahmad Fauzi, DashtArzhandi, M. Rezaei, Matsuura, T.
格式: Article
出版: Elsevier B.V. 2016
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在線閱讀:http://eprints.utm.my/id/eprint/72681/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84961613337&doi=10.1016%2fj.jngse.2016.03.053&partnerID=40&md5=beb4ad01e02bdd5842f57e1a8e00b9ea
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機構: Universiti Teknologi Malaysia
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總結:Porous hydrophobic polyvinylidene fluoride (PVDF) composite hollow fiber membranes were fabricated via phase inversion method by embedding different amounts of hydrophobic calcium carbonate (CaCO3) nano-particles in the polymer matrix. The effects of nano-particle loadings on the morphology, structure and performance of the spun membranes in gas-liquid contactors were investigated. The incorporation of hydrophobic nano-particles into the polymer network enabled the formation of more abundant and narrower finger-like pores in the composite membranes compared to plain PVDF membrane. Moreover, the addition of nano-particles enhanced the surface roughness, permeation rate, porosity and wettability resistance of the composite membranes. CO2 absorption performance of the fabricated membranes was evaluated via a gas-liquid membrane contactor system. The CO2 flux was improved to some extent by increasing the mixing ratio of CaCO3. Peak absorption performance of 1.52 × 10-3 mol m-2 s-1 at 300 ml/min absorbent flow rate was achieved when 20/100 weight ratio of CaCO3/PVDF was employed. However, further increase of the ratio resulted in a composite membrane with lower absorption performance than the other composite membranes. Moreover, a long-term stability study of the composite membrane with the best CO2 absorption flux showed no decline in performance in the initial 210 h of operation, indicating that the membrane possesses high potential for gas-liquid contactor applications.