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Dynamic PEM Fuel Cell Model for Power Electronics
Design with Temperature Consideration
Presented March 17th, 2006
by Ken Stanton
for:
Virginia Tech Ph.D. Qualifying Exam
Dr. Jaime De La Ree
Dr. Robert Hendricks
Dr. Doug Nelson
Presentation Outline
 Motivation
 Fuel Cell Modeling Background and Goals
 Temperature Dependency Background
 Load Dependent Model Discussion
 Parameters for the Electrical Model
 Simulation Results and Analysis
 Model Improvement Suggestions
 Conclusions
Motivation
 With energy costs constantly rising, alternative fuels like
hydrogen are a major focus
 Fuel cells are of great interest
 high efficiency
 minimal moving parts and no combustion
 produce only water vapor as emission (when H2 is fuel)
 To use fuel cell as source, power conditioning must be used
 To design power conditioning circuitry, a system model is
needed for simulation
 Goal of modeling the fuel cell is to simulate system
 PSpice is designed to simulate power electronics and electrical
loads
 It does not readily accept chemical or thermodynamic
equations, so we have to transform into electrical components
 Not all inputs to/effects of system are relevant – avoid
complexity and also improve simulation speed
Fuel Cell Modeling Background
DC/
AC
Fuel
Cell
DC/
DC
AC
Load
Vfc
+
vac
+
Vdc
––
Fuel Cell Modeling Background
 Complete formulae available for fuel cell parameters
 Electrical models would have to use equation blocks
 Simple electrical models have been developed
 Capture major static and dynamic terminal characteristics
 No extended properties – humidity, temperature, fuel quality
 Thorough PSpice and Simulink fuel cell models exist
 Very precise output
 Cumbersome, too many inputs, slow to simulate
 Time consuming to set up for different fuel cells
 Goal of this work is to incorporate as many terminal
characteristics as possible in the simplest form
Fuel Cell Test System
 For this testing, the Ballard Nexa
system was used
 1.2 kW peak output (43A at 28V)
 Pure H2 supplied at constant 7psi
 Ambient O2 supplied by variable
speed compressor
 Fully controlled by on-board digital
system
 Serial data logging connection to PC
Fuel Cell Modeling Goals - Static
 Fuel cell output voltage
deviates from ideal (E) due to
polarization losses
 Activation polarization is a
result of slow reaction
kinematics, primarily in cathode
 Vact = A ln(i/i0)
 Ohmic polarization losses are
result of conductors’ resistance
 Vohm = iReff
 Concentration polarization
occurs when reactants are used
up faster than they can diffuse
into cell
 Vconc = -B ln(1 – i/iL)
 V = E – Vact – Vohm – Vconc
(back)
Caisheng Wang et al (2005)
Fuel Cell Modeling Goals - Dynamic
 Voltage undershoot and
overshoot due to delay in air
compressor speed change
 Vcomp = 1 - e-t/t1
 Voltage reacts like capacitor
due to charge double-layer
effect
 Vcdl = e-t/t2 - 1
 Vdyn = Vcomp + Vcdl
0
10
20
30
40
50
60
0 2 4 6 8 10 12
t (sec)
0
500
1000
1500
2000
0 2 4 6 8 10 12
t (sec)
vFC(V)
iFC(A)
pFC(W)
Step load: 1.47kW
Parasitic load: 70W
voltage undershoot (2.5V)
due to compressor delay
150W dip
27.2V
300W power
overshoot
43V
Dynamic Circuit Model Using Purely
Electrical Circuit Components
 Diode models activation loss
 hact = A ln(i/i0)
 VD = nVT ln(ID/Is)
 Diode internal resistor
represents ohmic loss
 Transistor Q2 turns on in
concentration region
 Capacitor characterizes
charge double layer
 Inductor acts like
compressor coming up to
speed
Yuvarajan et al (APEC 2004)
Dynamic Circuit Model Using
Behavior Models
 Parasitic load of controls and
compressor added
 Dynamics simulated with
behavior models containing
time constants
 Fed into voltage controlled
voltage source which will
produce voltage transient
 Static voltage drops handled
mostly by resistances
Lai (SECA Review Meeting 2004)
Fuel Cell Modeling Goals
 The original goal was to add effects of temperature on output
 Temperature is not easily isolated nor predicted
 Exponential voltage response observed
 Primary cause is temperature change, but also humidity, hydration, and
other factors are influence
 Goal of this work is to make minor expansion to current model, incorporating
exponential voltage change over time
Temperature Dependency
Background
 Static equations previously shown have variations by
temperature (and more)
     
   
2 2
2
1
2
1 2 3 4
, , ,
0
limit
ln ln
2 2 2
ln ln
where
ln 1
ref H O
act O FC
ohm ohm a ohm membrane ohm c FC ohm
ohm ohm RI FC RT
FC
conc
G S RT
E T T P P
F F F
V T C I
V V V V I R
R R k I k T
IRT
V
zF I
   
       
 
    
 
   
  
 
  
 
Thermodynamics
 To predict the temperature of the fuel cell for use in the model,
the heat energy dynamics need to be observed
where
is power of chemical reaction
is electrical output power, V*I
is sensible and latent heat absorbed
is heat
FC FC net
net chem elec sens latent loss
chem
elec
sens latent
loss
dT
M C q
dt
q q q q q
q
q
q
q



   
&
& & & & &
&
&
&
& lost mainly due to air convection (increased by cooling fan)
Temperature Dependency - Summary
 Any finite load will induce a reaction in the fuel cell
 The chemical reaction releases energy
 Some of this energy is lost to the outside environment as heat
 Some is translated into electrical energy
 Remaining heat goes into fuel cell stack
 Fuel cell heating causes rise in temperature of stack
 Temperature is also altered by control system on Ballard system
 Changing temperature changes polarization losses
 Therefore, change in load causes change in temperature, which
in turn causes change in polarization voltage losses, and
therefore output voltage
Load Dependent Model
 Attempt to find relationship
between output power and
change in output voltage
 convenient for electrical model
 From testing, output voltage
can be 2.5V higher when stack
reaches full-load steady-state
on Ballard system
 This can greatly affect I-V curve
and therefore model accuracy
Stack Voltage Increase (V)
vs. Stack Output Power
with linear regression curve
V = 0.0022*P
0
1
2
3
4
5
0 500 1000 1500Power (W)
V(Volt)
Delta V
Linear (Delta V)
Voltage vs Current
When 2.2V/kW linear heating
relationship applied
27
29
31
33
35
37
39
41
43
45
0 5 10 15 20 25 30 35 40 45 50
Current Supplied (A)
Voltage
V
V + delV
Static (Steady-state) Load Conditions
 Output voltage and current
values are fed into multiply to
get power
 Gain factor is applied to
attain relationship between
voltage boost and output
power (2.2V/kW for Ballard)
 Result fed to voltage source
which boosts output voltage
 Note that this model does not
have any dynamic
components in it – purely for
I-V curve


X
+
Current Voltage
Static
Subsystem
Power
Dynamic Load Effects
 Output voltage of
stack changes
exponentially when
power demand is
altered
 As such, LaPlace
block added to
implement integral
and time delay of
load dynamics
 Note that all other
dynamics are present
+



X
+
+

+
X
+
Current Voltage
Dynamic
Subsystem
Power
Determining Time Constant
 To complete the model, a
time constant is required
 In base e exponential, time
constant equals rise time to
63% of final value
 Dozens of load curves were
recorded
 One major problem is built-in
cooling fan skews power-
temperature relationship
 Time constant is relatively
consistent for different
conditions
 50s chosen as constant
Simulation Results
 Plot on left is goal
 Blue curve from Ballard
 Red curve is Ballard + proposed linear gain
 Plot on right is simulation
 Lower curve matches Ballard well* – could use another ‘region’
 Upper curve simply follows linear trend
Voltage vs Current
When 2.2V/kW linear heating
relationship applied
27
29
31
33
35
37
39
41
43
45
0 5 10 15 20 25 30 35 40 45 50
Current Supplied (A)
Voltage
V
V + delV
Simulation Results
 Zero to full-load (1.2kW) step
 voltage dip created by the compressor lag
 gradual rise in voltage related to effect of temperature on fuel cell stack
 Simulation matches voltage curve well
 Difference in voltage levels due to age of fuel cell system
Simulation Results
 Four load steps show small voltage rises w/ stack loading (and heating)
 When load is removed, voltage falls off smoothly
 Times of load steps are same in simulation and actual test
 Loads: 225W, 360W, 480W, 680W
Model Improvement Suggestions
 Voltage “boost” approach shown here works, but is not as
representative as desired
 Perfect temperature model would have:
 Ambient temperature can be entered
 Temperature calculation*
 Temperature reduced by cooling fan*
 Value fed to model components*
 Each altered appropriately by temperature*
 Cold-start limitations added*
 True “thermal” heat energy handling
 Reasons this has not been reached
 Difficulty modeling all of above
 Difficulty with PSpice (* items above)
 May deviate too much from the original goal – to have a simple and fast-to-
simulate fuel cell model
Conclusions
 Previous models did not account for temperature transients of stack
 Voltage difference as much as 2.5V for Ballard system ~ 10%
 Implementation of basic temperature effects can be simple
 Create load dependent model
 Dynamics only need one more component than static
 All major fuel cell phenomenon are accounted for
 Power electronics designers can obtain output voltage and current from
this model and use it with confidence
Thank You!
Questions?

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Temperature model presentation

  • 1. Dynamic PEM Fuel Cell Model for Power Electronics Design with Temperature Consideration Presented March 17th, 2006 by Ken Stanton for: Virginia Tech Ph.D. Qualifying Exam Dr. Jaime De La Ree Dr. Robert Hendricks Dr. Doug Nelson
  • 2. Presentation Outline  Motivation  Fuel Cell Modeling Background and Goals  Temperature Dependency Background  Load Dependent Model Discussion  Parameters for the Electrical Model  Simulation Results and Analysis  Model Improvement Suggestions  Conclusions
  • 3. Motivation  With energy costs constantly rising, alternative fuels like hydrogen are a major focus  Fuel cells are of great interest  high efficiency  minimal moving parts and no combustion  produce only water vapor as emission (when H2 is fuel)  To use fuel cell as source, power conditioning must be used  To design power conditioning circuitry, a system model is needed for simulation
  • 4.  Goal of modeling the fuel cell is to simulate system  PSpice is designed to simulate power electronics and electrical loads  It does not readily accept chemical or thermodynamic equations, so we have to transform into electrical components  Not all inputs to/effects of system are relevant – avoid complexity and also improve simulation speed Fuel Cell Modeling Background DC/ AC Fuel Cell DC/ DC AC Load Vfc + vac + Vdc ––
  • 5. Fuel Cell Modeling Background  Complete formulae available for fuel cell parameters  Electrical models would have to use equation blocks  Simple electrical models have been developed  Capture major static and dynamic terminal characteristics  No extended properties – humidity, temperature, fuel quality  Thorough PSpice and Simulink fuel cell models exist  Very precise output  Cumbersome, too many inputs, slow to simulate  Time consuming to set up for different fuel cells  Goal of this work is to incorporate as many terminal characteristics as possible in the simplest form
  • 6. Fuel Cell Test System  For this testing, the Ballard Nexa system was used  1.2 kW peak output (43A at 28V)  Pure H2 supplied at constant 7psi  Ambient O2 supplied by variable speed compressor  Fully controlled by on-board digital system  Serial data logging connection to PC
  • 7. Fuel Cell Modeling Goals - Static  Fuel cell output voltage deviates from ideal (E) due to polarization losses  Activation polarization is a result of slow reaction kinematics, primarily in cathode  Vact = A ln(i/i0)  Ohmic polarization losses are result of conductors’ resistance  Vohm = iReff  Concentration polarization occurs when reactants are used up faster than they can diffuse into cell  Vconc = -B ln(1 – i/iL)  V = E – Vact – Vohm – Vconc (back) Caisheng Wang et al (2005)
  • 8. Fuel Cell Modeling Goals - Dynamic  Voltage undershoot and overshoot due to delay in air compressor speed change  Vcomp = 1 - e-t/t1  Voltage reacts like capacitor due to charge double-layer effect  Vcdl = e-t/t2 - 1  Vdyn = Vcomp + Vcdl 0 10 20 30 40 50 60 0 2 4 6 8 10 12 t (sec) 0 500 1000 1500 2000 0 2 4 6 8 10 12 t (sec) vFC(V) iFC(A) pFC(W) Step load: 1.47kW Parasitic load: 70W voltage undershoot (2.5V) due to compressor delay 150W dip 27.2V 300W power overshoot 43V
  • 9. Dynamic Circuit Model Using Purely Electrical Circuit Components  Diode models activation loss  hact = A ln(i/i0)  VD = nVT ln(ID/Is)  Diode internal resistor represents ohmic loss  Transistor Q2 turns on in concentration region  Capacitor characterizes charge double layer  Inductor acts like compressor coming up to speed Yuvarajan et al (APEC 2004)
  • 10. Dynamic Circuit Model Using Behavior Models  Parasitic load of controls and compressor added  Dynamics simulated with behavior models containing time constants  Fed into voltage controlled voltage source which will produce voltage transient  Static voltage drops handled mostly by resistances Lai (SECA Review Meeting 2004)
  • 11. Fuel Cell Modeling Goals  The original goal was to add effects of temperature on output  Temperature is not easily isolated nor predicted  Exponential voltage response observed  Primary cause is temperature change, but also humidity, hydration, and other factors are influence  Goal of this work is to make minor expansion to current model, incorporating exponential voltage change over time
  • 12. Temperature Dependency Background  Static equations previously shown have variations by temperature (and more)           2 2 2 1 2 1 2 3 4 , , , 0 limit ln ln 2 2 2 ln ln where ln 1 ref H O act O FC ohm ohm a ohm membrane ohm c FC ohm ohm ohm RI FC RT FC conc G S RT E T T P P F F F V T C I V V V V I R R R k I k T IRT V zF I                                   
  • 13. Thermodynamics  To predict the temperature of the fuel cell for use in the model, the heat energy dynamics need to be observed where is power of chemical reaction is electrical output power, V*I is sensible and latent heat absorbed is heat FC FC net net chem elec sens latent loss chem elec sens latent loss dT M C q dt q q q q q q q q q        & & & & & & & & & & lost mainly due to air convection (increased by cooling fan)
  • 14. Temperature Dependency - Summary  Any finite load will induce a reaction in the fuel cell  The chemical reaction releases energy  Some of this energy is lost to the outside environment as heat  Some is translated into electrical energy  Remaining heat goes into fuel cell stack  Fuel cell heating causes rise in temperature of stack  Temperature is also altered by control system on Ballard system  Changing temperature changes polarization losses  Therefore, change in load causes change in temperature, which in turn causes change in polarization voltage losses, and therefore output voltage
  • 15. Load Dependent Model  Attempt to find relationship between output power and change in output voltage  convenient for electrical model  From testing, output voltage can be 2.5V higher when stack reaches full-load steady-state on Ballard system  This can greatly affect I-V curve and therefore model accuracy Stack Voltage Increase (V) vs. Stack Output Power with linear regression curve V = 0.0022*P 0 1 2 3 4 5 0 500 1000 1500Power (W) V(Volt) Delta V Linear (Delta V) Voltage vs Current When 2.2V/kW linear heating relationship applied 27 29 31 33 35 37 39 41 43 45 0 5 10 15 20 25 30 35 40 45 50 Current Supplied (A) Voltage V V + delV
  • 16. Static (Steady-state) Load Conditions  Output voltage and current values are fed into multiply to get power  Gain factor is applied to attain relationship between voltage boost and output power (2.2V/kW for Ballard)  Result fed to voltage source which boosts output voltage  Note that this model does not have any dynamic components in it – purely for I-V curve   X + Current Voltage Static Subsystem Power
  • 17. Dynamic Load Effects  Output voltage of stack changes exponentially when power demand is altered  As such, LaPlace block added to implement integral and time delay of load dynamics  Note that all other dynamics are present +    X + +  + X + Current Voltage Dynamic Subsystem Power
  • 18. Determining Time Constant  To complete the model, a time constant is required  In base e exponential, time constant equals rise time to 63% of final value  Dozens of load curves were recorded  One major problem is built-in cooling fan skews power- temperature relationship  Time constant is relatively consistent for different conditions  50s chosen as constant
  • 19. Simulation Results  Plot on left is goal  Blue curve from Ballard  Red curve is Ballard + proposed linear gain  Plot on right is simulation  Lower curve matches Ballard well* – could use another ‘region’  Upper curve simply follows linear trend Voltage vs Current When 2.2V/kW linear heating relationship applied 27 29 31 33 35 37 39 41 43 45 0 5 10 15 20 25 30 35 40 45 50 Current Supplied (A) Voltage V V + delV
  • 20. Simulation Results  Zero to full-load (1.2kW) step  voltage dip created by the compressor lag  gradual rise in voltage related to effect of temperature on fuel cell stack  Simulation matches voltage curve well  Difference in voltage levels due to age of fuel cell system
  • 21. Simulation Results  Four load steps show small voltage rises w/ stack loading (and heating)  When load is removed, voltage falls off smoothly  Times of load steps are same in simulation and actual test  Loads: 225W, 360W, 480W, 680W
  • 22. Model Improvement Suggestions  Voltage “boost” approach shown here works, but is not as representative as desired  Perfect temperature model would have:  Ambient temperature can be entered  Temperature calculation*  Temperature reduced by cooling fan*  Value fed to model components*  Each altered appropriately by temperature*  Cold-start limitations added*  True “thermal” heat energy handling  Reasons this has not been reached  Difficulty modeling all of above  Difficulty with PSpice (* items above)  May deviate too much from the original goal – to have a simple and fast-to- simulate fuel cell model
  • 23. Conclusions  Previous models did not account for temperature transients of stack  Voltage difference as much as 2.5V for Ballard system ~ 10%  Implementation of basic temperature effects can be simple  Create load dependent model  Dynamics only need one more component than static  All major fuel cell phenomenon are accounted for  Power electronics designers can obtain output voltage and current from this model and use it with confidence