TY - JOUR
T1 - Nafion/TiO2 nanoparticle decorated thin film composite hollow fiber membrane for efficient removal of SO2 gas
AU - Park, Hyung Jin
AU - Bhatti, Umair Hassan
AU - Nam, Sung Chan
AU - Park, Sung Yeol
AU - Lee, Ki Bong
AU - Baek, Il Hyun
N1 - Funding Information:
This work was conducted under the framework of Research and Development Program of the Korea Institute of Energy Research (KIER) ( B8-2435 ).
Publisher Copyright:
© 2018 Elsevier B.V.
PY - 2019/3/18
Y1 - 2019/3/18
N2 - In this work, thin film nanocomposite (TFN) membranes for SO2 gas removal have been fabricated by incorporation of PEBAX and Nafion/TiO2 (hereafter referred as Nf/TiO2) nanoparticles on a polyethersulfone hollow fiber membrane substrate. Membrane structure, inner coating, and thickness were confirmed by SEM cross-sectional images. In addition, morphological and structural analyses of the membranes were performed using FTIR, SEM, EDX, TEM, and AFM. To investigate the effects of Nf/TiO2 nanoparticles on the gas permeation performance, four membrane modules with different mass concentrations of Nf/TiO2 – 0.025, 0.050, 0.075, and 0.1 g – were fabricated. The gas permeation experiments were performed with pure SO2, N2, and CO2 gases and a mixed gas (SO2/CO2/N2) within a pressure range of 1–3 bar and feed gas flow rate of 0.03–0.15 L/min. The obtained experimental results suggest that the addition of Nf/TiO2 nanoparticles improved the membrane performance by introducing sulfonate and hydroxyl functional groups to the membrane, and thus increased SO2 permeation and selectivity. The SO2 permeation was found to be 411–1671 GPU in the range of the studied parameters. The ideal selectivities achieved for SO2/N2 and SO2/CO2 were 2928 and 72, respectively. Overall, an SO2 removal efficiency of 93% was achieved by using the Nf/TiO2 incorporated TFN membrane.
AB - In this work, thin film nanocomposite (TFN) membranes for SO2 gas removal have been fabricated by incorporation of PEBAX and Nafion/TiO2 (hereafter referred as Nf/TiO2) nanoparticles on a polyethersulfone hollow fiber membrane substrate. Membrane structure, inner coating, and thickness were confirmed by SEM cross-sectional images. In addition, morphological and structural analyses of the membranes were performed using FTIR, SEM, EDX, TEM, and AFM. To investigate the effects of Nf/TiO2 nanoparticles on the gas permeation performance, four membrane modules with different mass concentrations of Nf/TiO2 – 0.025, 0.050, 0.075, and 0.1 g – were fabricated. The gas permeation experiments were performed with pure SO2, N2, and CO2 gases and a mixed gas (SO2/CO2/N2) within a pressure range of 1–3 bar and feed gas flow rate of 0.03–0.15 L/min. The obtained experimental results suggest that the addition of Nf/TiO2 nanoparticles improved the membrane performance by introducing sulfonate and hydroxyl functional groups to the membrane, and thus increased SO2 permeation and selectivity. The SO2 permeation was found to be 411–1671 GPU in the range of the studied parameters. The ideal selectivities achieved for SO2/N2 and SO2/CO2 were 2928 and 72, respectively. Overall, an SO2 removal efficiency of 93% was achieved by using the Nf/TiO2 incorporated TFN membrane.
KW - Gas separation
KW - Nafion/TiO
KW - PEBAX-1657
KW - Polyethersulfone
KW - Thin film nanocomposite (TFN) hollow fiber membrane
UR - http://www.scopus.com/inward/record.url?scp=85054452737&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2018.10.010
DO - 10.1016/j.seppur.2018.10.010
M3 - Article
AN - SCOPUS:85054452737
SN - 1383-5866
VL - 211
SP - 377
EP - 390
JO - Separation and Purification Technology
JF - Separation and Purification Technology
ER -