modelMassFlow0thOrderDynamics

PEMElectrolyzer mass flow as modeled by Espinosa, 2018

Extends from TransiEnt.Producer.Gas.Electrolyzer.Base.Physics.MassFlow.PartialMassFlow (partial model for PEM electrolyzer mass flow model).

Information

1. Purpose of model

This is a model to calculate mass flows in typical electrolyzers.

2. Level of detail, physical effects considered, and physical insight

Mass flow is modeled using expressions from Espinosa-López et al 2018. Dependent on stack current and Faraday's efficiency (1 by default).

3. Limits of validity

Original model developed and validated in the range of 20-60 °C with operating H2 and O2 tank pressure of 15-35 bar.

4. Interfaces

(no remarks)

5. Nomenclature

(no elements)

6. Governing Equations

Mass flow is modeled using Faraday's Law, as in Espinosa-López et al 2018.

7. Remarks for Usage

(no remarks)

8. Validation

Results have been validated against Espinosa-López et al 2018 published figures.

9. References

Manuel Espinosa-López, Philippe Baucour, Serge Besse, Christophe Darras, Raynal Glises, Philippe Poggi, André Rakotondrainibe, and Pierre Serre-Combe. Modelling and experimental validation of a 46 kW PEM high pressure water electrolyser. Renewable Energy, 119, pp. 160-173, 2018. doi: 10.1016/J.RENENE.2017.11.081.

10. Version History

Created by John Webster (jcwebste@edu.uwaterloo.ca) October 2018.

Parameters

TypeNameDefaultDescription
SI.MolarMassmolar_mass_H22.016e-3Molar mass of hydrogen gas
Integern_cellsnumber of cells in series
SI.Efficiencyeta_F1Faraday's efficiency, relating real H2 flow rate and theoretical

Components

TypeNameDefaultDescription
SI.MassFlowRatem_flow_H2 (from PartialMassFlow)mass flow rate of H2 gas
SI.MolarFlowRaten_flow_H2O (from PartialMassFlow)Molar consummation rate of water
SI.MolarFlowRaten_flow_H2 (from PartialMassFlow)Molar production rate of Hydrogen gas
SI.MolarFlowRaten_flow_O2 (from PartialMassFlow)Molar production rate of Oxygen gas
SI.Currenti_el_stackcurrent across the electrolyzer stack