Abstract
A steady-state model of green ammonia production using hydrogen produced from Polymer Electrolyte Membrane (PEM) electrolysis has been developed using ASPEN Plus Simulation software. Since the ASPEN plus does not offer the facility to directly model electrolysis cells, Aspen Custom Modeler (ACM) is used to develop the PEM stack. Stack is based on semi-empirical equations describing cell voltage and water transport across the membrane. The power requirement for electrolysis is expected to come from solar energy. This model of the PEM electrolyzer is integrated with the ammonia production model in a single flowsheet. With a power input of 4.25 kW, the PEM stack with 26 cells produced 0.048 kmol/h of H2. The corresponding ammonia production utilizing the conventional Haber–Bosch reactor was simulated to be 0.026 kmol/h. Such a model is expected to assist in the future design and scale-up of green ammonia processes.
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Abbreviations
- ∆H0:
-
Change in enthalpy at STP conditions
- Vcell:
-
Cell voltage
- Vopen circuit:
-
Open circuit voltage
- Vact_anode:
-
Activation overpotential at anode
- Vact_cathode:
-
Activation overpotential at cathode
- ΔG:
-
Change in Gibbs free energy
- ΔG*:
-
Gibbs free energy change at any temperature but standard pressure
- \(P_{{{\text{H}}_{2} }}\):
-
Partial pressure of H2
- \(P_{{{\text{O}}_{2} }}\):
-
Partial pressure of O2
- \(\alpha_{{{\text{H}}_{2} {\text{O}}}}\):
-
Activity coefficient of water (~ 1)
- Top:
-
Operating temperature
- i0,electrode:
-
Exchange current density, corresponding to the current density for the reversible semi-reaction at anode or cathode
- ielectrode:
-
Current density in the stack
- αelectrode:
-
Anode or cathode charge transfer coefficient
- n:
-
Number of electrons transferred in a half reaction
- F:
-
Faraday number
- iuseful:
-
Useful current density (found using faraday’s efficiency)
- icell:
-
Current density in cell (Istack/Acell)
- tan:
-
Thickness of anode
- tcat:
-
Thickness of cathode
- ρan:
-
Electrical resistivity of anode material
- ρcat:
-
Electrical resistivity of cathode material
- Acell:
-
Cell area
- tmem:
-
Membrane thickness
- σmem:
-
Conductivity of membrane
- λ:
-
Membrane humidification
- Ncell:
-
Number of cells in stack
- Neo:
-
Molar flow rate of water transported due to eo drag
- nd:
-
Electro-osmotic drag coefficient
- NDiff:
-
Molar flow rate of water transported due to diffusivity drag
- \(D_{{{\text{H}}_{2} {\text{O}},{\text{effective}}}}\):
-
Effective diffusivity
- Wstack:
-
Power consumption of electrolyzer stack
- σmem:
-
Membrane ionic conductivity
- Ɛ:
-
Porosity of membrane
- R:
-
Universal gas constant
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Natu, I., Arora, P. (2024). Modeling of Solar Ammonia Production Using ASPEN Plus. In: Hodge, BM., Prajapati, S.K. (eds) Proceedings from the International Conference on Hydro and Renewable Energy . ICHRE 2022. Lecture Notes in Civil Engineering, vol 391. Springer, Singapore. https://doi.org/10.1007/978-981-99-6616-5_7
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DOI: https://doi.org/10.1007/978-981-99-6616-5_7
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