TY - JOUR
T1 - Carbon composite membrane derived from a two-dimensional zeolitic imidazolate framework and its gas separation properties
AU - Zhong, Zhaoxiang
AU - Yao, Jianfeng
AU - Low, Ze-Xian
AU - Chen, Rizhi
AU - He, Ming
AU - Wang, Huanting
PY - 2014/6/1
Y1 - 2014/6/1
N2 - The carbonization of a newly reported two-dimensional zeolitic imidazolate framework (ZIF-L) with leaf-like morphology was investigated by TG, SEM, XRD and XPS. ZIF-L flakes were thermally stable at up to 200 °C, and completely transformed into an amorphous carbonaceous material after heat treatment in nitrogen at 550 °C. A carbon composite membrane was then prepared by deposition of ZIF-L flakes on a porous alumina support and then direct carbonization of ZIF-L film. During the carbonization, the ZIF-L membrane reorganized into a nanoporous carbon composite membrane composed of ZnO nanoparticles and leaf-like carbon flakes. The resulting nanoporous carbon composite membrane exhibited a narrow micropore size distribution, and it had higher BET surface area than the ZIF-L flakes. Gas separation permeation experiments showed that the carbon composite membrane had a high H2 permeance of 3.5 × 10−6 mol m−2 s−1 Pa−1, and moderate H2/N2 and H2/CO2 ideal selectivities of 6.2 and 4.9, respectively. This work presents a simple and effective method for preparing functional nanoporous carbon composite membranes from ZIFs (or MOFs) for many potential applications.
AB - The carbonization of a newly reported two-dimensional zeolitic imidazolate framework (ZIF-L) with leaf-like morphology was investigated by TG, SEM, XRD and XPS. ZIF-L flakes were thermally stable at up to 200 °C, and completely transformed into an amorphous carbonaceous material after heat treatment in nitrogen at 550 °C. A carbon composite membrane was then prepared by deposition of ZIF-L flakes on a porous alumina support and then direct carbonization of ZIF-L film. During the carbonization, the ZIF-L membrane reorganized into a nanoporous carbon composite membrane composed of ZnO nanoparticles and leaf-like carbon flakes. The resulting nanoporous carbon composite membrane exhibited a narrow micropore size distribution, and it had higher BET surface area than the ZIF-L flakes. Gas separation permeation experiments showed that the carbon composite membrane had a high H2 permeance of 3.5 × 10−6 mol m−2 s−1 Pa−1, and moderate H2/N2 and H2/CO2 ideal selectivities of 6.2 and 4.9, respectively. This work presents a simple and effective method for preparing functional nanoporous carbon composite membranes from ZIFs (or MOFs) for many potential applications.
UR - http://dx.doi.org/10.1016/j.carbon.2014.01.072
U2 - 10.1016/j.carbon.2014.01.072
DO - 10.1016/j.carbon.2014.01.072
M3 - Article
SN - 0008-6223
VL - 72
SP - 242
EP - 249
JO - Carbon
JF - Carbon
ER -