TY - JOUR
T1 - Membrane Based Gas-Liquid Dispersion Integrated in Fixed-Bed Reactor
T2 - A Highly Efficient Technology for Heterogeneous Catalysis
AU - Hou, Miaomiao
AU - Jiang, Hong
AU - Liu, Yefei
AU - Chen, Changlin
AU - Xing, Weihong
AU - Chen, Rizhi
N1 - Publisher Copyright:
© 2017 American Chemical Society.
PY - 2018/1/10
Y1 - 2018/1/10
N2 - A fixed-bed reactor with an external multichannel ceramic membrane for generation of gas-liquid microdispersion system is developed for heterogeneous catalysis. The reactor performance is evaluated by using glycerol hydrogenolysis to 1,2-propanediol over Cu-ZnO as the model reaction. Results highlight that the introduction of membrane with suitable pore size and channels is highly efficient for glycerol hydrogenolysis. Compared to the traditional feeding, the use of ceramic membrane allows a uniform microbubble-in-liquid dispersion system with higher gas holdup, and as a result, the glycerol conversion significantly increases from 84.9% to 97.4% with only half of the hydrogen consumption. The glycerol conversion of 92% and the 1,2-propanediol selectivity of 93% can be achieved in a 52 h continuous run. Our study demonstrates the advantages of the membrane dispersion based fixed-bed reactor in a continuous heterogeneous catalytic reaction.
AB - A fixed-bed reactor with an external multichannel ceramic membrane for generation of gas-liquid microdispersion system is developed for heterogeneous catalysis. The reactor performance is evaluated by using glycerol hydrogenolysis to 1,2-propanediol over Cu-ZnO as the model reaction. Results highlight that the introduction of membrane with suitable pore size and channels is highly efficient for glycerol hydrogenolysis. Compared to the traditional feeding, the use of ceramic membrane allows a uniform microbubble-in-liquid dispersion system with higher gas holdup, and as a result, the glycerol conversion significantly increases from 84.9% to 97.4% with only half of the hydrogen consumption. The glycerol conversion of 92% and the 1,2-propanediol selectivity of 93% can be achieved in a 52 h continuous run. Our study demonstrates the advantages of the membrane dispersion based fixed-bed reactor in a continuous heterogeneous catalytic reaction.
UR - http://www.scopus.com/inward/record.url?scp=85040452900&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.7b04184
DO - 10.1021/acs.iecr.7b04184
M3 - 文章
AN - SCOPUS:85040452900
SN - 0888-5885
VL - 57
SP - 158
EP - 168
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 1
ER -