TY - JOUR
T1 - Preparation of supported carbon membranes from furfuryl alcohol by vapor deposition polymerization
AU - Wang, Huanting
AU - Zhang, Lixiong
AU - Gavalas, George R.
PY - 2000/8/30
Y1 - 2000/8/30
N2 - Supported carbon membranes were prepared from furfuryl alcohol (FA) precursor by vapor deposition polymerization (VDP). For this purpose γ-Al2O3/α-Al2O3 or glass/α-Al2O3 support tubes were pretreated with an acid catalyst and exposed to FA vapors at 90°C. The tubes were then heated at 200°C to crosslink the poly(furfuryl alcohol) (PFFA) polymer and carbonized slowly to 600°C. The polymerization and carbonization cycle was repeated once to improve the permeation properties. The membranes were examined by scanning electron microscopy (SEM) and tested in a permeation cell with single gases (H2, N2, O2, CO2, CH4) and with the mixture CO2-CH4. After the first polymerization/carbonization cycle the membranes had little selectivity for gas separations. After the second polymerization/carbonization cycle the membranes had ideal selectivities 10-13 for O2:N2, 80-90 for CO2:CH4, and 90-350 for H2:N2 at room temperature. The permeance was 0.6-2.5 for H2, 0.27-0.58 for CO2 and 0.08 for O2, all in MPU (1MPU=10-8mol/m2Pas). The permeances were sharply higher at 150°C but the selectivities were lower, e.g. one of the membranes had H2 permeance 10.6MPU and H2:N2 ideal selectivity 30. Copyright (C) 2000 Elsevier Science B.V.
AB - Supported carbon membranes were prepared from furfuryl alcohol (FA) precursor by vapor deposition polymerization (VDP). For this purpose γ-Al2O3/α-Al2O3 or glass/α-Al2O3 support tubes were pretreated with an acid catalyst and exposed to FA vapors at 90°C. The tubes were then heated at 200°C to crosslink the poly(furfuryl alcohol) (PFFA) polymer and carbonized slowly to 600°C. The polymerization and carbonization cycle was repeated once to improve the permeation properties. The membranes were examined by scanning electron microscopy (SEM) and tested in a permeation cell with single gases (H2, N2, O2, CO2, CH4) and with the mixture CO2-CH4. After the first polymerization/carbonization cycle the membranes had little selectivity for gas separations. After the second polymerization/carbonization cycle the membranes had ideal selectivities 10-13 for O2:N2, 80-90 for CO2:CH4, and 90-350 for H2:N2 at room temperature. The permeance was 0.6-2.5 for H2, 0.27-0.58 for CO2 and 0.08 for O2, all in MPU (1MPU=10-8mol/m2Pas). The permeances were sharply higher at 150°C but the selectivities were lower, e.g. one of the membranes had H2 permeance 10.6MPU and H2:N2 ideal selectivity 30. Copyright (C) 2000 Elsevier Science B.V.
KW - Furfuryl alcohol
KW - Supported carbon membranes
KW - Vapor deposition polymerization
UR - http://www.scopus.com/inward/record.url?scp=0034734319&partnerID=8YFLogxK
U2 - 10.1016/S0376-7388(00)00444-0
DO - 10.1016/S0376-7388(00)00444-0
M3 - 文章
AN - SCOPUS:0034734319
SN - 0376-7388
VL - 177
SP - 25
EP - 31
JO - Journal of Membrane Science
JF - Journal of Membrane Science
IS - 1-2
ER -