TY - JOUR
T1 - A feasibility assessment of a retrofit Molten Carbonate Fuel Cell coal-fired plant for flue gas CO2 segregation
AU - Cooper, R.
AU - Bove, D.
AU - Audasso, E.
AU - Ferrari, M. C.
AU - Bosio, B.
PY - 2021/4/21
Y1 - 2021/4/21
N2 - This work considers the use of a Molten Carbonate Fuel Cell (MCFC) system as a power generation and CO2 concentrator unit downstream of the coal burner of an existing production plant. In this way, the capability of MCFCs for CO2 segregation, which today is studied primarily in reference to large-scale plants, is applied to an intermediate-size plant highlighting the potential for MCFC use as a low energy method of carbon capture. A technical feasibility analysis was performed using an MCFC system-integrated model capable of determining steady-state performance across varying feed composition. The MCFC user model was implemented in Aspen Custom Modeler and integrated into the reference plant in Aspen Plus. The model considers electrochemical, thermal, and mass balance effects to simulate cell electrical and CO2 segregation performance. Results obtained suggest a specific energy requirement of 1.41 MJ kg CO2−1 significantly lower than seen in conventional Monoethanolamine (MEA) capture processes.
AB - This work considers the use of a Molten Carbonate Fuel Cell (MCFC) system as a power generation and CO2 concentrator unit downstream of the coal burner of an existing production plant. In this way, the capability of MCFCs for CO2 segregation, which today is studied primarily in reference to large-scale plants, is applied to an intermediate-size plant highlighting the potential for MCFC use as a low energy method of carbon capture. A technical feasibility analysis was performed using an MCFC system-integrated model capable of determining steady-state performance across varying feed composition. The MCFC user model was implemented in Aspen Custom Modeler and integrated into the reference plant in Aspen Plus. The model considers electrochemical, thermal, and mass balance effects to simulate cell electrical and CO2 segregation performance. Results obtained suggest a specific energy requirement of 1.41 MJ kg CO2−1 significantly lower than seen in conventional Monoethanolamine (MEA) capture processes.
KW - Aspen custom modeler
KW - Carbon capture
KW - Fuel cell applications
KW - MCFC process Simulation
UR - http://www.scopus.com/inward/record.url?scp=85093660001&partnerID=8YFLogxK
U2 - 10.1016/j.ijhydene.2020.09.189
DO - 10.1016/j.ijhydene.2020.09.189
M3 - Article
AN - SCOPUS:85093660001
VL - 46
SP - 15024
EP - 15031
JO - International journal of hydrogen energy
JF - International journal of hydrogen energy
SN - 0360-3199
IS - 28
ER -