TY - GEN
T1 - Modeling and optimization of a fast fluidized bed reactor for carbonation reactions
AU - Chen, Jhao Rong
AU - Wu, Wei
N1 - Publisher Copyright:
© 2017 IEEE.
PY - 2017/7/18
Y1 - 2017/7/18
N2 - A carbonator is described as a fast fluidized bed reactor to capture CO2. The proposed mathematical model is validated by literatures and experimental data. In our approach, the bed temperature and inventory weight are used to optimize the reactor design and the water gas shift (WGS) reaction with calcium oxide improves the hydrogen production under the modified WGS kinetics. It is validated that the carbonation can break the chemical equilibrium of WGS and make the reaction go forward to reduce CO and generate a quantity of hydrogen gas.
AB - A carbonator is described as a fast fluidized bed reactor to capture CO2. The proposed mathematical model is validated by literatures and experimental data. In our approach, the bed temperature and inventory weight are used to optimize the reactor design and the water gas shift (WGS) reaction with calcium oxide improves the hydrogen production under the modified WGS kinetics. It is validated that the carbonation can break the chemical equilibrium of WGS and make the reaction go forward to reduce CO and generate a quantity of hydrogen gas.
UR - http://www.scopus.com/inward/record.url?scp=85034092290&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=85034092290&partnerID=8YFLogxK
U2 - 10.1109/ADCONIP.2017.7983855
DO - 10.1109/ADCONIP.2017.7983855
M3 - Conference contribution
AN - SCOPUS:85034092290
T3 - 2017 6th International Symposium on Advanced Control of Industrial Processes, AdCONIP 2017
SP - 642
EP - 647
BT - 2017 6th International Symposium on Advanced Control of Industrial Processes, AdCONIP 2017
PB - Institute of Electrical and Electronics Engineers Inc.
T2 - 6th International Symposium on Advanced Control of Industrial Processes, AdCONIP 2017
Y2 - 28 May 2017 through 31 May 2017
ER -
