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Fuel Cell Modeling In AMESim IMAGINE Specific Thermodynamic Applications 04/2006 Cédric ROMAN – [email protected]

Fuel Cell Modeling In AMESim - sft.asso.fr · ROMAN Cédric – [email protected] Power Based Fuel Cell Applications 3 1 10 100 1k 10k 100k 1M 10M

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Fuel Cell Modeling In AMESim

IMAGINE Specific Thermodynamic Applications 04/2006 Cédric ROMAN – [email protected]

ROMAN Cédric – [email protected]

2 Introduction

  Fuel Cells are complex multi-domain dynamic systems   Electrical, electrochemical, fluidic, thermal

phenomena are coupled   Controlling such systems is a challenge to

ensure efficiency and reliability   Modelling fuel cells systems implies

  Interoperability   Multi-disciplinary and dynamic simulation

environment

ROMAN Cédric – [email protected]

3 Power Based Fuel Cell Applications

1 10 100 1k 10k 100k 1M 10M

Portable electronics equipment

Cars, boats, and domestic

CHP

Distributed power generation,

CHP, also buses

Potential for zero emissions,

higher efficiency

Higher efficiency, less pollution,

quiet

AFC

PEMFC

SOFC

MCFC

Typical applications

Power (W)

Main advantages

Range of application of the different types of FC

ROMAN Cédric – [email protected]

4 Typical Fuel Cell PEM Control System

ROMAN Cédric – [email protected]

5 Typical Fuel Cell PEM Control System

ELECTRICAL SUB-SYSTEM

ROMAN Cédric – [email protected]

6 Typical Fuel Cell PEM Control System

ELECTRICAL SUB-SYSTEM

ROMAN Cédric – [email protected]

7 Typical Fuel Cell PEM Control System

PNEUMATIC SYSTEM

ROMAN Cédric – [email protected]

8 Typical Fuel Cell PEM Control System

PNEUMATIC SYSTEM

ROMAN Cédric – [email protected]

9 Typical Fuel Cell PEM Control System

COOLING SYSTEM

ROMAN Cédric – [email protected]

10 Typical Fuel Cell PEM Control System

COOLING SYSTEM

ROMAN Cédric – [email protected]

11 Typical Fuel Cell PEM Control System

STACK SYSTEM

ROMAN Cédric – [email protected]

12 Introduction

  State of the art of PEMFC stack numerical models   Dynamic model of analogic electrical equivalent

system   Pneumatics and chemicals are modelled with equivalent

electric elements

  Quasi-steady state model based on CFD code   Limited by boundary conditions   CPU cost: days on parallelized clusters

  Bond-Graph model   Multi-domain (electrical/chemical/pneumatic)

ROMAN Cédric – [email protected]

13 Stack System   AMESim Model for stack modelling

  Inspired from Bond Graph   Physical model of electrical, electrochemical,

pneumatic and thermal phenomena   Stack design and optimization   Dynamic modelling of pneumatics, chemical

reactions, etc…

ROMAN Cédric – [email protected]

14

Diffusion Protonic resistance

PEM cell Model structure (Explanations)

membrane CL GDL

width

length/nel

heigth

x

y

H+ H+ H+ H+ H+

O2

O2 O2 O2

O2

Porous media

Catalyst

Conductive

flow rate

Protons from anodic reaction

gas mixture (O2,N2,H2O)

Cathode side

ROMAN Cédric – [email protected]

15

Current prediction

&

Ohmic losses

PEM cell Model structure (Explanations)

membrane CL GDL

e- e- e- e- e-

H2O H2O H2O H2O H2O

Electrochemical reaction

Nernst equation

Reaction kinetic

Diffusion

ROMAN Cédric – [email protected]

16 PEMFC Stack Model

  Core of model   electrochemical reaction

  Interfaces   Electrical circuit   Electrolyte   Catalyst layer

Electrical circuit

Catalyst layer

Electrolyte (membrane)

  Reaction parameters   Stoechiometry in data file

  Reference heat of formation, standard entropy   Kinetic parameters in data file

  Partial orders, kinetic constant   Assymetry parameter

ROMAN Cédric – [email protected]

17 PEMFC Stack model

  PEMFC cathode   Electrochemical reaction   Gas mixture equilibrium

potential   Nernst equation

  Overpotential   Activation Voltage

– Equilibrium potential   = Disequilibrium

  Reaction kinetic   Butler-Volmer equation

ROMAN Cédric – [email protected]

18 PEMFC Stack model

  Gas mixture description  Dynamic description  Mixture of N species   Perfect gas equation of state

 Real gas possible   Thermodynamic description

  JANAF 71: Cp, h, u, s given by 5 order polynomial of temperature   Validity domain (200<->5000K)

 Diffusion  Binary coefficients / Wilke formula

 Water condensation/vaporisation (to come…)

Predefined species

ROMAN Cédric – [email protected]

19 PEMFC Stack model

Add-on Gas Mixture

Basic Elements approach

Powerful features Initialisation facility

Compatibility with PCD/PN/THPN

ROMAN Cédric – [email protected]

20 PEMFC Stack model

Add-on Fuel Cells

Basic Elements approach

Compatible with Add-on Gas Mixture

Thermal libraries

ROMAN Cédric – [email protected]

21 PEMFC Stack model

  Possible Discretizations

Catalyst layer Gas diffusion layer

Channel

7 nodes 13 nodes

ROMAN Cédric – [email protected]

22 PEMFC Stack model

Diffusion in

porous media

Thermal Exchange

Diffusion in

porous media

Electrochemical reaction

Ohmic losses

Double Capacitanc

e layer

Laminar flow in channel

ROMAN Cédric – [email protected]

23 PEMFC Stack model

80 Nodes Model

Serpentine configuration

ROMAN Cédric – [email protected]

24

AMESim Simulation  Comparison of different architectures (different flowcharts)  Design of the control of the PEMFC System  Start-up process

 freeze start  Change of load

 Drive cycle  Power demand

PEMFC system simulation

Power demand

ROMAN Cédric – [email protected]

25 PEMFC AMESim model

  Allow quick results   Physical model   Transient behaviour   Gas diffusion efficiency   Thermal management

  Robustness & Risk analysis   AMESim features

  Monte-Carlo simulation   Design of experiment   Optimization

Sensitivity Analysis

ROMAN Cédric – [email protected]

26 PEMFC AMESim model

  Gain Time & Performance

  Have a better understanding of physics

  Use all powerfuls AMESim applications   Compatible with standard libraries   Activity index   Linear analysis (Bode, Nyquist, Nichols,…)   Design of Experiment / Optimization   Real-time