TY - JOUR
T1 - Energy, exergy, exergoeconomic, and environmental (4E) analyses of a combined system comprising reformed methanol high-temperature proton exchange membrane fuel cells and absorption refrigeration cycle
AU - Zhong, Zhaoda
AU - Zhu, Jimin
AU - Li, Na
AU - Liu, Wei
AU - Gao, Lei
AU - Gao, Xin
AU - Simon Araya, Samuel
AU - Liso, Vincenzo
PY - 2024
Y1 - 2024
N2 - 4E (energy, exergy, exergoeconomic, and environmental) analyses of a reformed methanol high-temperature proton exchange membrane fuel cell (RM HT-PEMFC) system identify inefficiencies, assess associated costs, and evaluate environmental impacts. However, such studies remain limited in the literature, particularly those exploring the impact of the operating parameters of the methanol steam reforming in the combined RM HT-PEMFC and single-effect absorption refrigeration cycle (ARC). This study addresses this gap by analyzing a tri-generation consisting of the RM HT-PEMFC and the single-effect ARC. Simulation results indicate a total exergy destruction of 21.65 kW, a total cost rate of 8.93 $/h, an exergoeconomic factor of 43.22%, and an exergy efficiency of 33.06% in the baseline case. Notably, the stack and burner account for the highest irreversibility, contributing 67.75% of total exergy destruction and 55.71% of the total cost rate. Parametric studies on four key variables–current density, stack temperature, reformer temperature, and steam-to-carbon ratio–reveal that higher system exergy efficiency is generally associated with lower carbon dioxide emissions. Uncertainty analysis shows that extending the HT-PEMFC’s lifespan to 40,000 h can reduce exergy cost per unit product by 16.23%, while decreasing the price of green methanol to 11.00 $/h can lower costs by 26.97%.
AB - 4E (energy, exergy, exergoeconomic, and environmental) analyses of a reformed methanol high-temperature proton exchange membrane fuel cell (RM HT-PEMFC) system identify inefficiencies, assess associated costs, and evaluate environmental impacts. However, such studies remain limited in the literature, particularly those exploring the impact of the operating parameters of the methanol steam reforming in the combined RM HT-PEMFC and single-effect absorption refrigeration cycle (ARC). This study addresses this gap by analyzing a tri-generation consisting of the RM HT-PEMFC and the single-effect ARC. Simulation results indicate a total exergy destruction of 21.65 kW, a total cost rate of 8.93 $/h, an exergoeconomic factor of 43.22%, and an exergy efficiency of 33.06% in the baseline case. Notably, the stack and burner account for the highest irreversibility, contributing 67.75% of total exergy destruction and 55.71% of the total cost rate. Parametric studies on four key variables–current density, stack temperature, reformer temperature, and steam-to-carbon ratio–reveal that higher system exergy efficiency is generally associated with lower carbon dioxide emissions. Uncertainty analysis shows that extending the HT-PEMFC’s lifespan to 40,000 h can reduce exergy cost per unit product by 16.23%, while decreasing the price of green methanol to 11.00 $/h can lower costs by 26.97%.
KW - Economic
KW - exergoeconomic
KW - high-temperature proton exchange membrane fuel cell
KW - thermodynamic
KW - waste heat recovery
U2 - 10.1080/15567036.2024.2429750
DO - 10.1080/15567036.2024.2429750
M3 - Journal article
SN - 1556-7036
VL - 46
SP - 16642
EP - 16656
JO - Energy Sources, Part A: Recovery, Utilization and Environmental Effects
JF - Energy Sources, Part A: Recovery, Utilization and Environmental Effects
IS - 1
ER -