TY - JOUR
T1 - Composite-alumina-carbon molecular sieve membranes prepared from novolac resin and boehmite. Part I
T2 - Preparation, characterization and gas permeation studies
AU - Llosa Tanco, Margot A.
AU - Pacheco Tanaka, David A.
AU - Rodrigues, Sandra C.
AU - Texeira, Miguel
AU - Mendes, Adélio
N1 - Publisher Copyright:
Copyright © 2015, Hydrogen Energy Publications, LLC.
PY - 2015/5/4
Y1 - 2015/5/4
N2 - Abstract Supported composite alumina-carbon molecular sieve membranes (c-CMSM) were prepared from in house prepared novolac phenolic resin loaded with boehmite nanoparticles in a single dipping-drying-carbonization step. A porous α-alumina tube support was dipped into a N-methyl-2-pyrrolidone solution containing polymerized novolac resin loaded with boehmite, subsequently dried at 100 C and carbonized at 500 C under nitrogen environment. The structure, morphology and performance of the membranes were examined by scanning electron microscopy (SEM), X-ray diffraction (XRD), thermogravimetric analysis (TGA), carbon dioxide adsorption and permeation of N2, O2, He, H2 and CO2. SEM showed carbon membranes with a thin and very uniform layer with a thickness of ca. 3 μm CO2 adsorption isotherms indicated that the produced carbon membranes presented a microporous structure. The c-CMSM exhibited good gas separation properties. The permselectivity surpass the Robeson upper bound for polymeric membranes, especially regarding ideal permselectivities of pairs H2/N2 = 117, and He/O2 = 49. Aging effects were observed after membrane exposure to ambient air. However with a thermal treatment under nitrogen atmosphere the permeance of nitrogen increases.
AB - Abstract Supported composite alumina-carbon molecular sieve membranes (c-CMSM) were prepared from in house prepared novolac phenolic resin loaded with boehmite nanoparticles in a single dipping-drying-carbonization step. A porous α-alumina tube support was dipped into a N-methyl-2-pyrrolidone solution containing polymerized novolac resin loaded with boehmite, subsequently dried at 100 C and carbonized at 500 C under nitrogen environment. The structure, morphology and performance of the membranes were examined by scanning electron microscopy (SEM), X-ray diffraction (XRD), thermogravimetric analysis (TGA), carbon dioxide adsorption and permeation of N2, O2, He, H2 and CO2. SEM showed carbon membranes with a thin and very uniform layer with a thickness of ca. 3 μm CO2 adsorption isotherms indicated that the produced carbon membranes presented a microporous structure. The c-CMSM exhibited good gas separation properties. The permselectivity surpass the Robeson upper bound for polymeric membranes, especially regarding ideal permselectivities of pairs H2/N2 = 117, and He/O2 = 49. Aging effects were observed after membrane exposure to ambient air. However with a thermal treatment under nitrogen atmosphere the permeance of nitrogen increases.
KW - Carbon membranes
KW - Composite membranes
KW - Gas separation
KW - Nanoparticles
KW - Novolac
KW - Phenolic resin
UR - http://www.scopus.com/inward/record.url?scp=84926408489&partnerID=8YFLogxK
U2 - 10.1016/j.ijhydene.2015.02.112
DO - 10.1016/j.ijhydene.2015.02.112
M3 - Article
AN - SCOPUS:84926408489
SN - 0360-3199
VL - 40
SP - 5653
EP - 5663
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
IS - 16
M1 - 15527
ER -