Frano Barbir - Ruđer Bošković Institute · PDF filelocal electrochemical impedance...

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Transcript of Frano Barbir - Ruđer Bošković Institute · PDF filelocal electrochemical impedance...

Frano Barbir Pictorial Resume

energy partners

Diagnosis noun

Investigation or analysis of the cause or

nature of a condition, situation or problem

Diagnostic(s) noun

the art or practice of diagnosis

Diagnostics in fuel cell development process

design

fabricate

test

model

Knowledge:

materials

processes

interactions

requirements

diagnostics

Should

it work?

Does

it work?

Diagnostics in fuel cell development process

Diagnostics in control development process

Diagnostics in fuel cell development process

Diagnostics in control development process

Diagnostics in operation

controller

fuel cell

control

element

measurement

sensor/

transmitter

process

variable

manipulated

variable

controller

output

signal

measured

value

disturbances

error

set point

measured

process

variable

signal

Observe (voltage/current, pressure drop, temperature)

0

0,1

0,2

0,3

0,4

0,5

0,6

0,7

0,8

0,9

1

0 20 40 60 80 100 120

Observe (voltage/current, pressure drop, temperature)

Change a parameter and compare

First fuel cell law:

One cannot change only one parameter in a fuel cell —

change of one parameter causes a change in at least

two other parameters, and at least one of them has an

opposite effect of the one expected to be seen.

F. Barbir, PEM Fuel Cells Theory and Practice, Elsevier/Academic Press, 2005

nm m mm m

Fuel cells: Problems at different scales

12700 km 12.7 km 12.7 m 12.7 mm

Observe (voltage/current, pressure drop, temperature)

Change a parameter and compare

Disturb and observe Small disturbances

Large disturbances (exaggerate or accelerate)

controller

fuel cell

control

element(s)

diagnostics

process

variable(s)

manipulated

variable(s)

controller

output

signal(s) controller

action

signal

desired/expected

state of health

diagnosis

measured

values

disturbances

Diagnostics in fuel cell development process

Diagnostics in control development process

Diagnostics in operation

Post mortem diagnostics

Online

Offline

Post mortem

Electrochemical techniques Polarization curve

Current interruption

Electrochemical Impedance

Spectroscopy

Cyclic Voltammetry

CO Stripping Voltammetry

Linear Sweep Voltammetry

Current Distribution Mapping Partial MEA

Segmented Cells

Species Distribution Mapping Pressure Drop Measurements

Gas Composition Analysis

Neutron Imaging

Magnetic Resonance Imaging

X-ray Imaging

Optically Transparent Fuel Cells

Embedded Sensors

Temperature Distribution Mapping IR Transparent Fuel Cells

Embedded Sensors

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

0

0.2

0.4

0.6

0.8

1

1.2

0 500 1000 1500 2000

current density (mA/cm²)

cell

po

ten

tial

(V)

activation losses

resistance losses

mass transport

losses resulting V vs. i curve

theoretical (ideal) voltage

0

0.2

0.4

0.6

0.8

1

1.2

0 500 1000 1500 2000

current density (mA/cm²)

ce

ll p

ote

nti

al

(V)

normal polarization

curve

higher resistance

drying?

mass transport problems

flooding?

hgher activation losses

Data should be taken at multiple current or voltage points.

Typical points would be open circuit and 5 or 6 points between 600 mV/cell and

850 mV/cell,

15 minutes dwell at each point

The data from the last five (5) minutes should be averaged and then plotted as

average current versus average voltage.

Protocol on Fuel Cell Components Testing

Polarization curve sweep

Qiangu Yan, J. Power Sources, Vol 161, 2006, pp 492–502

Presented at IECEC, Portsmouth, VA, August 12, 2003

Static Feed UNIGEN Cycle Test (Total 8/1/03 3:00 PM - 147 cycles)Electrolysis: 60 min @ 200 ASF; Fuel Cell: 40 min @ 300 ASF

160 F, 50-75 psig

0.50

0.70

0.90

1.10

1.30

1.50

1.70

1.90

2.10

2.30

2.50

50.00 50.50 51.00 51.50 52.00 52.50 53.00 53.50 54.00 54.50 55.00

Elapsed Time (hr)

Ce

ll V

olt

ag

e/D

iffe

ren

tia

l P

res

su

re

> 100 LEO cycles

Fuel Cell

40 min

Electrolysis

60 min

M. Weiland, Int. J. Hydrogen Energy,

2012, in print

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

Polarization curve at cell temperature 80°C

anode/cathode humidifier temperatures 80/60°C

hydrogen/air, 30 psig, H2 stoich 1.5, air stoich 5.0

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

ce

ll p

ote

nti

al

(V

)

0 200 400 600 800 1000 current density (mA/cm²)

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

Source: T.P. Ralph and M.P. Hogarth, Platinum Metals Review, Vol. 46, No. 1, pp. 3-14, 2002

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

A

Current interrupt method for measurement of fuel cell resistance

Fuel cell Load

Digital osciloscope

voltage

time

Immediate rise in

voltage, VR

Slow rise to OCV

Vact

Time of current interrupt

Cell voltage before

current interrupt

OCV

Current interrupt method for measurement of fuel cell resistance

voltage

time

Immediate rise in

voltage, VR

Time of current interrupt

Cell voltage before

current interrupt

OCV

discrete points

extrapolated straight lines

ringing effect

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

Nyquist and Bode plots

R

HF Resistance

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

0.2

0.3

0.4

0.5

0.6

0.7

2000 2500 3000 3500 4000 4500 5000

Time (seconds)

Ce

ll P

ote

ntia

l (V

olts),

Re

sis

tan

ce

(m

iliO

hm

-cm

2),

Pre

ssu

re D

rop

(10

kP

a)

20

30

40

50

60

70

80

Te

mp

era

ture

(oC

)

Pressure Drop

Humidification

Temperature

Stack Temperature

Cell Voltage

Resistance

0.2

0.3

0.4

0.5

0.6

0.7

10000 10500 11000 11500 12000 12500

Time (seconds)

Cell

Pote

ntial (V

olts),

Resis

tance (

mili

Ohm

-cm

2),

Pre

ssure

Dro

p (

10 k

Pa)

20

40

60

80

Tem

pera

ture

(oC

)Humidification

Temperature

Stack Temperature

Cell Voltage

Pressure Drop

Resistance

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

S.J.C. Cleghorn, C.R. Derouin, M.S. Wilson,

and S. Gottesfeld, A Printed Circuit Board

Approach to Measuring Current Distribution in

a Fuel Cell, J. Appl. Electrochem., 1997

L

o

k

a

l

e

M

e

s

s

u

n

g

e

n

local current density measurement

dynamic > 2000 measurement /s

local temperature measurement

local electrochemical

impedance spectroscopy (EIS)

4 mm

D. Derteisen et al., Int. J. Hydrogen Energy,

Vol 37, 2012, pp. 7736–7744

D. Derteisen et al., Int. J. Hydrogen Energy,

Vol 37, 2012, pp. 7736–7744

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

iR camera

Temperature Mapping with iR Camera

smallest sensor

on the market

Sensirion SHT 71

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

X Liu, et al. Water flooding and two-

phase flow in cathode channels of

proton exchange membrane fuel cells,

Journal of Power Sources,

Straight Channels

Interdigitated Flow Field

D. Lee, J. Bae, Visualization of flooding in a single cell and stacks by using a newly-

designed transparent PEMFC International Journal of Hydrogen Energy, Vol. 37,

No.1, 2012, pp 422–435

S Basu et al., J Power Sources, Vol 162, 2006, pp 286–293

Inukai, J. et al. Direct Visualization of Oxygen Distribution in Operating Fuel Cells.

Angew. Chem. Int. Ed. 47, 2792–2795 (2008).

K Takada et al. J. Power Sources , Vol 196, 2011, Pages 2635–2639

Polarization curve

Polarization curve hysteresis

Comparative polarization curves

Current interrupt

AC impedance spectroscopy

Pressure drop

Current density mapping

Temperature mapping

Flow visualization

Neutron/X-Ray imaging

Real time detection

of liquid water inside

an operating fuel cell

A. Turhan, K. Heller, J.S. Brenizer and M.M. Mench, Passive control of liquid water storage and distribution

in a PEFC through flow-field design, Journal of Power Sources 180 (2) (2008), pp. 773–783.

at Penn State University

H. Markötter et al., Int. J. Hydrogen Energy,

Vol 37, 2012, pp. 7757–7761

P. Deevanhxay, Electrochemistry Comm., 2012

http://dx.doi.org/10.1016/j.elecom.2012.05.028,

Diagnostics – important aspect of fuel cell R&D

Limited number of diagnostic methods applicable

for fuel cell control purposes

Definition of optimum performance must include

life time

In order to achieve optimum performance diagnostics

is crucial for prognostics and health management

Conclusions

PEM Fuel Cells: Theory and Practice

More information about PEM fuel cells:

Frano Barbir

PEM Fuel Cells: Theory and Practice

Elsevier/Academic Press, 2005

ISBN 978-0-12-078142-3

Available from:

www.elsevier.com

www.amazon.com

www.barnesandnoble.com

Written as a textbook

for engineering students.

Used at hundreds of universities

In U.S., China, India, Korea, Iran,

Germany, Croatia …

New updated edition coming out 2012!