TY - JOUR
T1 - Using poly(N,N-dimethylaminoethyl methacrylate)/polyacrylonitrile composite membranes for gas dehydration and humidification
AU - Du, Jennifer Runhong
AU - Liu, Li
AU - Chakma, Amit
AU - Feng, Xianshe
PY - 2010/8/15
Y1 - 2010/8/15
N2 - The transport of water vapor through a composite membrane consisting of hydrophilic poly(N,. N-dimethylaminoethyl methacrylate) (PDMAEMA) as the active layer and polyacrylonitrile (PAN) as the substrate was investigated, and the performance of the membrane for gas dehydration and humidification applications was evaluated. For gas dehydration, methane/water vapor mixtures were used as feed and vacuum was applied on the downstream side. The feed composition and operating temperature were found to have a significant effect on the membrane performance. The PAN substrate had little effect on the permeation of methane, but the resistance of the substrate to water vapor permeation was significant because of the substantially higher permeability of water vapor in the membrane. For gas humidification, liquid water was brought to be in contact with the active layer of the membrane and nitrogen gas flowed on the other side. With an increase in the gas flow rate, the mass transfer rate of water through the membrane to reach the gas stream increased, and the humidity level of the gas stream decreased. The humidification can be enhanced significantly by operating at a higher temperature. A phenomenological mass transfer equation was derived for membrane humidifiers to correlate the overall mass transfer coefficient and membrane area, and this equation could be used in process design and scale up.
AB - The transport of water vapor through a composite membrane consisting of hydrophilic poly(N,. N-dimethylaminoethyl methacrylate) (PDMAEMA) as the active layer and polyacrylonitrile (PAN) as the substrate was investigated, and the performance of the membrane for gas dehydration and humidification applications was evaluated. For gas dehydration, methane/water vapor mixtures were used as feed and vacuum was applied on the downstream side. The feed composition and operating temperature were found to have a significant effect on the membrane performance. The PAN substrate had little effect on the permeation of methane, but the resistance of the substrate to water vapor permeation was significant because of the substantially higher permeability of water vapor in the membrane. For gas humidification, liquid water was brought to be in contact with the active layer of the membrane and nitrogen gas flowed on the other side. With an increase in the gas flow rate, the mass transfer rate of water through the membrane to reach the gas stream increased, and the humidity level of the gas stream decreased. The humidification can be enhanced significantly by operating at a higher temperature. A phenomenological mass transfer equation was derived for membrane humidifiers to correlate the overall mass transfer coefficient and membrane area, and this equation could be used in process design and scale up.
KW - Composite membrane
KW - Gas dehydration
KW - Humidification
KW - Natural gas
KW - Poly(N,N-dimethylaminoethyl methacrylate)
KW - Water permeation
UR - http://www.scopus.com/inward/record.url?scp=77954386916&partnerID=8YFLogxK
U2 - 10.1016/j.ces.2010.05.005
DO - 10.1016/j.ces.2010.05.005
M3 - Article
AN - SCOPUS:77954386916
SN - 0009-2509
VL - 65
SP - 4672
EP - 4681
JO - Chemical Engineering Science
JF - Chemical Engineering Science
IS - 16
ER -