Abstract
Syngas fuel such as hydrogen and carbon monoxide generated by solar energy is a promising method to use solar energy and overcome its fluctuation effectively. This study proposes a combined cooling, heating, and power system using the reversible solid oxide fuel cell assisted by solar energy to produce solar fuel and then supply energy products for users during the period without solar radiation. The system runs a solar-assisted solid oxide electrolysis cell mode and a solid oxide fuel cell mode. The thermodynamic models are constructed, and the energetic and exergetic performances are analyzed. Under the design work conditions, the SOEC mode’s overall system energy and exergy efficiencies are 19.0% and 20.5%, respectively. The electrical, energy and exergy efficiencies in the SOFC mode are 51.4%, 71.3%, and 45.2%, respectively. The solid oxide fuel cell accounts for 60.0% of total exergy destruction, caused by the electrochemical reactions’ thermodynamic irreversibilities. The increase of operating temperature of solid oxide fuel cell from 800 °C to 1050 °C rises the exergy and energy efficiencies by 11.3% and 12.3%, respectively. Its pressure from 0.2 to 0.7 MPa improves electrical efficiency by 13.8% while decreasing energy and exergy efficiencies by 5.2% and 6.0%, respectively.
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Abbreviations
- Abs:
-
absorber
- ARS:
-
absorption refrigeration system
- C:
-
condenser
- CCHP:
-
combined cooling heating and power
- COP:
-
coefficient of performance
- E:
-
evaporator
- HG:
-
high pressure generation
- HX:
-
heat exchanger
- HTX:
-
high temperature heat exchanger
- LHV:
-
low heat value
- LG:
-
low pressure generation
- LTX:
-
low temperature heat exchanger
- MRS:
-
methane reforming reaction
- ORC:
-
organic Rankine cycle
- PV:
-
photovoltaic
- PTSC:
-
parabolic trough solar collectors
- RGibbs:
-
gibbs reactor
- RStoic:
-
stoichiometric rector
- R U :
-
reactant utilization ratio
- RWGS:
-
reverse water gas shift
- SOCs:
-
solid oxide cells
- SOFC:
-
solid oxide fuel cell
- SOEC:
-
solid oxide electrolysis cell
- WGS:
-
water gas shift
- A :
-
area/m2
- Ex :
-
the specific exergy/kW
- ex :
-
the exergy ratio/kJ·kmol−1
- e :
-
electrode porosity
- E n :
-
Nernst voltage/V
- E an :
-
activation energy of anode/kJ·mol−1
- E :
-
activation energy of cathode/kJ·mol−1
- F :
-
Faraday constant/K·kmol−1
- H :
-
Enthalpy/kJ
- h :
-
the specific enthalpy/kJ·kmol−1
- G :
-
electrical energy demand/kJ·kmol−1
- J :
-
current/A
- j :
-
current density/A·m−2
- k :
-
the pre-exponential factor/A·m−2
- M :
-
the mass flow rate/kg·h−1
- m :
-
the mole flow rate/kmol·h−1
- N :
-
solid oxide fuel cell quantity
- P :
-
power/kW
- P :
-
pressure/MPa
- R :
-
universal gas constant, 8.314 kJ/(kmol·K)
- r :
-
mean radius of electrode pore/m
- T :
-
temperature/°C
- t :
-
thickness/m
- U :
-
fuel utilization of fuel cell
- V :
-
voltage/V
- W :
-
the electrical power/kW
- α :
-
conversion rate/%
- δ :
-
molar fraction/%
- η :
-
efficiency/%
- Λ:
-
irreversibility loss
- ω :
-
concentration
- act:
-
the activation over potential
- avg:
-
average
- an:
-
the anode of fuel cell
- ca:
-
the cathode of fuel cell
- comp:
-
compressor
- cell:
-
fuel cell
- conc:
-
the concentration over potential
- che:
-
chemical
- chilled:
-
chilled water
- dhw:
-
domestic hot water
- des:
-
the destruction of exergy
- ele:
-
the electricial power
- en:
-
the specific energy
- ex:
-
the specific exergy
- heat:
-
heat output
- in:
-
input
- inv:
-
dc-ac inverter
- net:
-
the net power output
- OP:
-
operating
- ohmic:
-
the ohmic over potential
- out:
-
output
- phy:
-
physical exergy
- tur:
-
turbine
- 0:
-
the state of ambient environment
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Acknowledgments
This research has been supported by the National Natural Science Foundation of China (Grant No. 51876064 and 52090064) and the Bureau of Shihezi Science & Technology (Grant No. 2021ZD02).
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Gao, Y., Yao, W., Wang, J. et al. Thermodynamic Analysis of Solid Oxide Fuel Cell Based Combined Cooling, Heating, and Power System Integrated with Solar-Assisted Electrolytic Cell. J. Therm. Sci. 32, 93–108 (2023). https://doi.org/10.1007/s11630-022-1680-z
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DOI: https://doi.org/10.1007/s11630-022-1680-z