DR.S.RADHAKRISHNAN DR.S.RADHAKRISHNAN NCL , PUNE NCL , PUNE - - PowerPoint PPT Presentation

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DR.S.RADHAKRISHNAN DR.S.RADHAKRISHNAN NCL , PUNE NCL , PUNE - - PowerPoint PPT Presentation

DR.S.RADHAKRISHNAN DR.S.RADHAKRISHNAN NCL , PUNE NCL , PUNE s.radhakrishnan@ s.radhakrishnan@ ncl.res.in ncl.res.in Flow Pattern FUEL CELL CONSTRUCTION AND BIPOLAR PLATES FLOW OF GASES / VAPOURS IN FUEL CELLS Graphite Plate Graphite


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SLIDE 1

DR.S.RADHAKRISHNAN DR.S.RADHAKRISHNAN NCL , PUNE NCL , PUNE s.radhakrishnan@ ncl.res.in s.radhakrishnan@ ncl.res.in

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SLIDE 2

FUEL CELL CONSTRUCTION AND BIPOLAR PLATES

Flow Pattern

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SLIDE 3

FLOW OF GASES / VAPOURS IN FUEL CELLS Graphite Plate Graphite Plate

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SLIDE 4

IMPORTANT FUNCTIONS OF BIPOLAR PLATES IN FUEL CELLS

1. MECHANICAL SUPPORT FOR THE MEMBRANE ASSEMBLY 2. PROVIDE FLOW CHANNELS FOR THE FUEL : HYDROGEN OR METHANOL AS WELL AS COOLANT / WATER 3. SEPARATE INDIVIDUAL CELLS 4. PROVIDE BACK TO BACK ELECTRICAL CONNECTION TO CELLS / STACK AS WELL AS EXTERNAL LEADS/ BUS BARS 5. TRANSFER HEAT AWAY FROM THE CELL

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SLIDE 5

IMPORTANT PROPERTIES OF BIPOLAR PLATES WHICH CONTROL THE PERFORMANCE OF FC :

  • 1. HIGH ELECTRICAL CONDUCTIVITY
  • 2. CONTACT RESISTANCE SHOULD BE LOW
  • 3. ROBUST MECHANICAL PROPERTIES WITH

SURFACE HARDNESS

  • 4. HIGH THERMAL CONDUCTIVITY
  • 5. FLOW PATTERN UNIFORM AND SMOOTH
  • 6. MACHINABLE / MOLDABLE
  • 7. LOW PERMEABILITY TO GASES
  • 8. LOW WATER ABSORPTION / CORROSION
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SLIDE 6

IMPORTANCE OF BIPOLAR PLATES IN COST AND EFFICIENCY OF FC :

  • 1. BIPOLAR PLATES COMPRISE THE

MAXIMUM PORTION OF THE FC : WEIGHT AND VOLUME IS ALMOST 70% OF TOTAL

  • 2. ANY NEW DESIGN OF THE FC HAS TO

START FIRST IN THE BIPLOAR PLATES

  • 3. MORE THAN 30% OF THE COST OF THE FC

IS IN BIPLOAR PLATES US GOVT.REPORT 2004 :

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SLIDE 7

MATERIALS OF BIPOLAR PLATES :

  • 1. PRECIOUS METALS WERE USED IN VERY

EARLY DAYS

  • 2. GRAPHITE BECAME VERY POPULAR FOR

THIS APPLICATION IN LATER VERSIONS

  • 3. CONDUCTING POLYMER COMPOSITES ARE

THE LATEST MATERIALS USED IN THESE PLATES

  • 4. CONDUCTING POLYMER CORROSION

RESISTANT COATING FORMULATIONS : FUTURE FUEL CELLS

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SLIDE 8

MATERIALS OF BIPOLAR PLATES : GRAPHITE IS MOST COMMON Structure of Graphite : Hexagonal : Most common Rhombohedral Diamond Cubic

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SLIDE 9

BIPOLAR PLATES MATERIAL : GRAPHITE IS MOST COMMONLY USED Structure of Natural Graphite :

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SLIDE 10

BIPOLAR PLATES MATERIAL : GRAPHITE IS MOST COMMONLY USED Properties of Graphite : (range of different grades)

Property Unit Value Density g/cc 1.3 – 1.95 Porosity % 0.7 - 53 Modulus of Elasticity GPa 8 - 15 Compressive strength MPa 20 - 200 Flexural strength MPa 7 - 100 Thermal conductivity W/m K 25 - 470 Specific Heat J/kg K 710 - 830 Thermal exp. Co- efficient m/m K 2.2 - 6.0 x 10 -4 Electrical resistivity

  • hm-m

5 to 30 x 10 –6

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SLIDE 11

CONVENTIONAL METHOD FOR FARBICATING BIPOLAR PLATES

Special Graphite Powder Press in to form of thick sheets High temperature sinter Machine to form flow pattern on both sides USING CNC MACHINE Impregnate with resin for reducing porosity

Bipolar Plates

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SLIDE 12

ROLE OF FLOW FIELD / CHANNELS ON BIPOLAR PLATES:

  • 1. ALLOW INPUT OF FUEL AND BRING IT IN

CONTACT WITH CATALYST ACTIVATED ELECTRODE

  • 2. ALLOW THE COUNTER PART GAS

(OXYGEN) AND BRING IT IN CLOSE PROXIMITY OF MEA

  • 3. DRAIN OFF WATER FORMED
  • 4. CONDUCT AWAY HEAT THROUGH

COOLANT FLOW

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SLIDE 13

FLOW FIELD DESIGNS: Straight Radial Serpentine

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SLIDE 14

FLOW FIELD DESIGNS:

Design (a) shows rapid decrease in performance than (b). Flow field design plays a major role in removing the product water and the excess condensed water effectively

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SLIDE 15

FLOW FIELD DESIGNS: DESIGN IS NEEDED TO BE OPTIMIZED BY TAKING INTO ACCOUNT THE FOLLOWING :

  • ACTIVE AREA OF THE PLATE
  • GAS FLOW RATE
  • PRESSURE DROP
  • RESIDENCE TIME REQUIRED FOR CONVERSION
  • AMOUNT OF WATER FORMATION
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SLIDE 16

BIPOLAR PLATES MATERIAL : GRAPHITE IS MOST COMMONLY USED Properties of Graphite Bipolar Plates : (Du Pont)

Property Test Method Unit Value Specific gravity ASTM D792 g/cc 1.85

  • Perp. Resistance

DOC A128 Ohm-cm 0.03-0.04 Tensile strength ASTM D638 MPa 25 Flexural strength ASTM D790 MPa 53 Compressive creep ASTM D2990 Strain% 0.02 Impact strength ASTM D256 Ft;lb/in 0.14 Thermal cond. Hot Disc W/m K 43

  • Max. Use Temp

TMA C 210

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SLIDE 17

BIPOLAR PLATES MATERIAL : Oak Ridge Laboratory USA reports Carbon/carbon composite bipolar plates Slurry-molded fabrication of carbon/carbon composite material lends itself to low-cost, high-volume production Hydrogen/oxygen flowfields can be stamped into the carbon composite preform Increased conductivity, lighter weight, and greater corrosion resistance than graphite plates Porvair Fuel Cell Technology has taken up this for commercialization ( it is not yet available)

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SLIDE 18

DRAWBACKS OF EXISTING MATERIAL AND METHODS : High Temperatures / Energy inputs needed : Graphite itself is made by high temperature. Plates have to be sintered at HT Material is not mechanically sturdy : easily damaged during handling, assembly etc. Limited in processing : Not easy to shape or machine as required Large amount of wastage of material ( during track machining, moulding etc.) CONTACT RESISTANCE arises due to limitation on tightening / application of pressure Batch process hence large scale production difficult HIGH COST

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SLIDE 19

ALTERNATIVE MATERIALS AND PROCESSES :

  • Conducting Polymer Composites are most

suitable for Bipolar Plates

  • Injection moulding, compression moulding are

employed

  • Prefabricated Steel with Corrosion resisting

coating with conducting polymers

  • Conducting Polymer Screen Printing the Pattern

for micro fuel cells on various substrates

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SLIDE 20

CONDUCTING POLYMERS:

There are basically three types of conducting polymers :

  • 1. Conducting Polymer Composites (CPC) : Electronic
  • 2. Inherently Conducting Polymers (ICP) : Electronic
  • 3. Solid Polymer Electrolytes (SPE) : Ionic

ALL ARE USEFUL FOR FUEL CELLS

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SLIDE 21

CONDUCTING POLYMER COMPOSITES :

  • Conducting Polymer Composites are made by

incorporation of conducting particles in a polymer matrix.

  • Polymer Matrix : can be thermoplastic or

thermosetting

  • Conducting Particles : can be graphite, carbon

black, carbon fiber, metal particles etc.

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SLIDE 22

CONDUCTING POLYMER COMPOSITE BIPOLAR PLATES

CONDUCTING POLYMER COMPOUND INJECTION MOULDING AS BLANK SHEETS OR IN SPECIAL MOULDS READY BIPOLAR PLATES WITH INBUILT PATTERN

HOT STAMPING OF SHEETS FOR PATTERN

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SLIDE 23

COMPOSITIONAL DEPENDENCE OF CONDUCTIVITY

Adding conducting particles to plastics to give CPC Simple rule

  • f mixtures

Percolation type (Actual)

  • CONC. Φ

L

  • g

σ σ φ1 φ2

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SLIDE 24

EFFECT OF PARTICLE SHAPE ON RESISTIVITY IN POLYMER COMPOSITES : σm = σh [ (φ - φ c ) / ( 1 - φ c ) ] t for φ > φ c σm = σ1 [ ( φ c - φ ) / φ c ] -s for φ c < φ Percolation theory gives : t = (1 - φ c ) / (1 – L 1) = φ c / Lh = 1 / ( 1 – L 1 + L h ) for oriented ellipsoids t = m 1 ( 1- φ c ) = m h φ c = m 1 m h /( m 1 + m h ) for randomly dispersed ellipsoids

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SLIDE 25

EFFECT OF PARTICLE SHAPE ON RESISTIVITY IN POLYMER COMPOSITES : Percolation theory :

Cp = Pc Z Cp : critical number of contacts / particle Pc : critical probability of network formation Z : maximum number of contacts possible for the geometry

Lattice Z φm Pc Cp FCC 12 0.74 0.125 1.5 BCC 8 0.68 0.183 1.46 Simple Cubic 6 0.82 0.254 1.52 Diamond 4 0.34 0.389 1.56 Random 6

  • .637
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SLIDE 26

EFFECT OF PARTICLE SHAPE ON RESISTIVITY IN POLYMER COMPOSITES :

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SLIDE 27

EFFECT OF PARTICLE SHAPE ON RESISTIVITY IN POLYMER COMPOSITES : Effect of aspect ratio on φ c

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SLIDE 28

EFFECT OF PARTICLE SHAPE ON RESISTIVITY IN POLYMER COMPOSITES :

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SLIDE 29

EFFECT OF THIRD COMPONENT ON RESISTIVITY IN POLYMER COMPOSITES :

PPS-Graphite-CB 1.E-01 1.E+00 1.E+01 1.E+02 1.E+03 1.E+04 10 20 30 40 50 60 Graphite Conc.(%) Log Resistance(ohms)

Graphite -PPS Graphite-5%CB-PPS

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SLIDE 30

EFFECT OF THIRD COMPONENT ON RESISTIVITY IN POLYMER COMPOSITES :

PES-Graphite-CB

1.E-01 1.E+00 1.E+01 1.E+02 1.E+03 1.E+04 1.E+05 1.E+06 1.E+07 10 20 30 40 50 60 Graphite Conc.(%) Log Resistance(ohms)

Graphite -PES Graphite-5%CB-PES

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SLIDE 31

Conductivity of hybrid conducting composite plates:

Effect of addition of third component on Conductivity Without With

Graphite-PES-Carbon Black

1.E-01 1.E+00 1.E+01 1.E+02 1.E+03 1.E+04 1.E+05 1.E+06 1.E+07 10 20 30 40 50 60 Graphite Conc.(%) Log Resistance(ohms)

Graphite -PES Graphite-5%CB-PES

SPIC PLATE

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SLIDE 32

ANISOTROPY IN RESISTIVITY IN GRAPHITE POLYMER COMPOSITES :

1.0E-01 1.0E+00 1.0E+01 1.0E+02 1.0E+03 1.0E+04 1.0E+05 1.0E+06 1.0E+07 1.0E+08 1.0E+09 1.0E+10 1.0E+11 10 20 30 40 50 60 % Graphite in PEEK Resistance (ohm)

Resistance Perpendicular (ohm) Resistance Parallel (ohm)

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SLIDE 33

ANISOTROPY IN RESISTIVITY IN GRAPHITE POLYMER COMPOSITES :

1.0E-01 1.0E+01 1.0E+03 1.0E+05 1.0E+07 1.0E+09 1.0E+11 10 20 30 40 50 60 % Graphite in PES Resistance (ohm)

Resistance Perpendicular (ohm) Resistance Parallel (ohm)

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SLIDE 34

PROCESSING OF BIPOLAR PLATES TECHNIQUE DEPENDS ON THE NATURE OF POLYMER MATRIX: Thermoplastic : Injection / Compression Molding Thermosetting : Hand lay up / Compression ,, Polymer + Graphite+ additive Mixing :

  • 1. Powder Processing
  • 2. Solution Blending
  • 3. Melt extrusion
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SLIDE 35

PROCESSING OF BIPOLAR PLATES POLYMERS USED FOR MAKING COMPOSITES THERMOPLASTIC POLYMERS : Polypropylene, TPO, PET,PVDF, PS copolymer for FC operating temperature < 100 C PPS, PES, PEEK, LCP blends for FC operating at 150 C Graphite has to be incorporated by melt compounding using sigma mixer and twin screw extruder having high capacity of loading Melt flow is necessary for the graphite incorporated compound

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SLIDE 36

PROCESSING OF BIPOLAR PLATES POLYMERS USED FOR MAKING COMPOSITES: THERMOSETTING POLYMERS / RESINS Aliphatic polyesters, phenol formaldehyde , epoxies, modified epoxy etc cross-linked with agents Graphite is incorporated in low molecular weight semi-liquid resin by sigma blender or two roll mill Cross-linking agent is added and the mix partially cured or directly poured in the moulds Partially cured mix ( B stage cured) is compression moulded at high temperature for fast and final cure

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SLIDE 37

VISCOSITY OF POLYMERS WITH FILLERS EQUATIONS FOR VISCOSITY η= ηf (1+ 2.5φ) Einstein ηr = [1+1.25 φ(1- φ/φm)] 2 Eiler ηr = e KE φ / (1- φ / φm ) Mooney ηr = (1- φ/φm) –[ K

E ] φ m Krieger and Dougherty

ηr = (1- φ/φm) –2 Quemada

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SLIDE 38

RELATIVE VISCOSITY OF LDPE + CB

LDPE / Carbon Black

0.5 1 1.5 2 2.5 3 3.5 0.1 0.2 0.3 0.4 0.5 0.6 0.7

  • Vol. Fraction of C-B

ln (ηr)

ln hr (Einstein) ln hr (Eilers) (0.637) ln hr (Mooney) (0.637) ln hr (K&D) (0.637) ln hr (Exp)

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SLIDE 39

RELATIVE VISCOSITY OF POLYMERS WITH FILLERS

VISCOSITY OF POLYMERS INCREASES TREMENDOUSLY WITH ADDTION OF FILLERS

MFI Comparison

0.2 0.4 0.6 0.8 1 20 40 60 % Content MFI (g/10min)

PAni-DBSA PAni-HCl Carbon Black

η α (1/MFI) , ηr = [ηblend / η0 ] =(MFI)0 / (MFI)blend MFI 5 Kg

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SLIDE 40

VISCOSITY OF POLYMERS + FILLERS + ADDITIVES

Reduction in percolation threshold + increase in flow by using processing aid (PEO)

1.00E

  • 16

1.00E

  • 14

1.00E

  • 12

1.00E

  • 10

1.00E

  • 08

1.00E

  • 06

1.00E

  • 04

10 20 30 40 50 % P A N I Conductivity (S/cm)

with out additives with 5phr P E O with 5phr P E G

Krieger & Dougherty Vs. Blends with different PEO contents

0.5 1 1.5 2 2.5 0.1 0.2 0.3 0.4 0.5 0.6 0.7 Volum e fraction of PA NI ln (ηr)

ln hr (K&D ) (0.74) ln hr (with 5phr P E O) ln hr (with 3phr P E O)

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SLIDE 41

TESTING THE MOULD DESIGN USING MOLD FLOW PACKAGE FOR TWO POLYMERS (PES) AND PP POLYPROPYLENE REPOL MELT TEMP 230 C POLYETHER SULFONE GAFONE MELT TEMP 380 C

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SLIDE 42

Injection Moulded Bipolar Plate :

Injection Molded samples with PP +carbon black :

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SLIDE 43

Compression Moulded Bipolar Plate :

Compression Molded samples with PP +carbon black

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SLIDE 44

INJECTION MOULDED PLATE :

Injection Molded samples with PP +carbon black : Flow Channel Track depth Variation Pattern 0.53 0.52 0.52 0.52 0.52 0.54 0.53 0.56 0.55 0.61 0.52 0.55 0.55 0.57

0.51

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SLIDE 45

Dimensional changes :

Shrinkage PES

  • 10

10 20 30 20 40 60 80 Graphite Conc.(%) S h r in k a g e (% )

Shrinkage PEEK

  • 2

2 4 6 8 20 40 60 80 Graphite Conc. (%) S h r in k a g e

Shrinkage Studies

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SLIDE 46

Dimensional changes during processing :

Shrinkage Studies

Shrinkage PPS

  • 5

5 10 15 20 40 60 80 Graphite Conc. (%) Shrinkage (%)

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SLIDE 47

EFFECT OF BLENDING METHOD ON PROPERTIES :

PES-Graphite Composites 1.00E-01 1.00E+01 1.00E+03 1.00E+05 1.00E+07 20 40 60 80 Wt % Graphite LogResistance ( Ohm ) Perpendicular- Powder Perpendicular- Solution Blending

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SLIDE 48

PES-Graphite Composites 1.00E-01 1.00E+01 1.00E+03 1.00E+05 1.00E+07 1.00E+09 1.00E+11 20 40 60 80 Wt % Graphite LogResistance ( Ohm ) Parallel-Pow der parallel-Solution Blending

EFFECT OF BLENDING METHOD ON PROPERTIES :

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SLIDE 49

EFFECT OF BLENDING METHOD ON PROPERTIES :

Anisotropy of Graphite- PES

1 2 3 20 40 60 80 Wt% Graphite Rperp/Rpll S P

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SLIDE 50

XRD Of PES- Graphite Powder Blended Composite :

22 23 24 25 26 27 28 29 30 10000 20000 30000

Unsintered Sintered

Intensity (cps) 2 Theta

10% Graphite

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SLIDE 51

22 24 26 28 30 5000 10000 15000 20000 25000 30000

Intensity (cps) 2 Theta

After Before 45% Graphite

XRD of PES-Graphite Solution Blended :

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SLIDE 52

22 24 26 28 30

  • 5000

5000 10000 15000 20000 25000 30000 35000 40000

Intensity (cps) 2 Theta

After Before 60%Graphite

XRD of PES-Graphite Solution Blended :

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SLIDE 53

Wt % Graphite Crystallite Size (nm) Interplanar d- spacing ( Ao) Before sintering After sintering Before sintering After sintering 37.50 46.20 21.92 3.3560 3.3923 44.44 41.67 17.34 3.3646 3.4438 60.00 20.83 13.86 3.3796 3.4623

XRD ANALYSIS :

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SLIDE 54

POSSIBLE REARRANGEMENT OF GRAPHITE PARTICLES :

Powder Processed Solution Processed

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SLIDE 55

PROPERTIES OF POLYMER COMPOSITE PLATES (BULK MOULING COMPOUND) :

BMCI Vinyl Ester Fuel-Plate Com pounds ( Com pression Molding)

Grade Filler Application BMC 9 4 0 -8 5 9 6 Graphite ( Bipolar Plate)

BMC 8 4 5 3 0 % glass ( End Plate) Electrical Conductivity, S/ cm Through Plane ( Z) I n Plane ( X-Y) 7 0 9 5 — — Specific Gravity Shrinkage, in./ in. Flexural Strength, psi Flexural Modulus, 1 0 6 psi Un-notched I zod, ft-lb/ in. Com pressive Creep, % 1 0 0 0 hr@8 0 C Therm al Conductivity, V/ m -K UL Flam e Rating 1 .8 2 0 .0 0 1 6 8 0 0 a 1 .7 0 .5 0 .3 c 1 6 9 4 V-O 1 .8 0 .0 0 1 2 ,0 0 0 b 1 .6 7 .0 2 .0 d — 9 4 V-O

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SLIDE 56

I njection m olding technology has yet to overcom e the current preference for com pression m olding to m ake therm oset fuel- cell plates.

Quantum 's Prem tex Vinyl Ester Bipolar Plate Com pound

( Com pression Molding)

Electrical Conductivity, S/ cm Through Plane ( Z) I n Plane ( X-Y) 2 5 9 6 Specific Gravity Shrinkage, in./ in. Flexural Strength, psi Fluxural Modulus, 1 0 6 psi Com pressive Strength, psi Glass Transition Tem p., C Therm al Conductivity, W / m -K ( through plane) UL Flam e Rating 1 .8 0 -0 .0 0 1 5 6 5 0 0 1 .7 7 8 0 0 1 7 5 1 8 9 4 V-O

Volume 13 - No. 2 Bulk Molding Compounds, Inc. October, 2001

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SLIDE 57

PROPERTIES OF POLYMER COMPOSITE PLATES (BULK MOULING COMPOUND) :

Quantum 's Prem tex Vinyl Ester Bipolar Plate Com pound ( Com pression Molding)

Electrical Conductivity, S/ cm Through Plane ( Z) I n Plane ( X-Y) 2 5 9 6 Specific Gravity Shrinkage, in./ in. Flexural Strength, psi Flexural Modulus, 1 0 6 psi Com pressive Strength, psi Glass Transition Tem p., C Therm al Conductivity, W / m -K ( through plane) UL Flam e Rating 1 .8 0 -0 .0 0 1 5 6 5 0 0 1 .7 7 8 0 0 1 7 5 1 8 9 4 V- O

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SLIDE 58

Du Pont's new fuel Cells Business is about to launch a graphic-filled LCP com pound for injection m olded bipolar plates.

PLASTICS ENGINEERING 2003

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SLIDE 59

Granules containing graphite After injection molding POWER 2004 ZBT INJECTION MOLDED PLATES AND STACK

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SLIDE 60

Properties of Moulded Plate (NCL)

Property Units Value with > 90% Gr Experimental with < 45% Gr Bulk Density g/cc < 1.8 1.3 Flexural Strength MPa 40

  • Compressive Strength

MPa 50

  • Thermal Conductivity

W/mK 10 5 Electrical Resistivity (with carbon contact at 3.0 Mpa load) Ohm- cm 5 x 10 -2 4.2 x 10 -1 Roughness variation over 30 x20 (channel depth variation) 0.65 mm 0.55 ±0.02 Maximum Operating Temperature (continuous)

  • C

150 110 Surface hardness Shore D Scale 62 68

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SLIDE 61

SECOND ROUTE TO MAKE BIPOLAR PLATES :

PRE-FABRICATE THIN METAL PLATES WITH PATTERN DEPOSITE CONDUCTING CARBON OR OTHER HYBRID MATERAL BASED COATING SANDWICH STRUCTURE

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SLIDE 62

CONDUCTING POLYMER COMPOSITE COATED SS FOILS FOR BIPOLAR PLATES: MEA MEA

L L L

H2 H2 H2 H2 O2 O2 O2 O2 STAMPED + COATED PLATE TYPICAL SINGLE CELL ASSEMBLY WITH PREFORMED SS FOIL WITH CONDUCTING CORROSION RESISTANT COATING SEALING

NEW APPROACH TO MAKE THINNER BIPOLAR PLATES

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SLIDE 63

CONDUCTING POLYMER COMPOSITE COATED STEEL FOILS FOR BIPOLAR PLATES:

  • 1. CONDUCTING POLYANILINE SYNTHEZED

ON BULK SCALE (1 Kg)

  • 2. DISPERSION COATING FORMULATIONS

MADE

  • 3. SS PLATES DIP COATED , DRIED, BAKED

AT 55-60 C AND TESTED FOR CORROSION

  • 4. TESTING ENVIRONMENT : 60 C, 3.5 Saline
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SLIDE 64

ACCELERATED CORROSION TESTING OF PANI COATINGS :

  • 11
  • 10
  • 9
  • 8
  • 7
  • 6
  • 5
  • 4
  • 3
  • 0.6
  • 0.1

0.4 0.9

Potential(mV) log I/A

3 day 1 day Initial 6 day 15 day

0% PANI +PVAc +ZnO 2% PANI +PVAc + ZnO

  • 10
  • 9
  • 8
  • 7
  • 6
  • 5
  • 0.6
  • 0.4
  • 0.2

0.2

Potential/V log i/A Initial 15 day 1 day 3 day 6 day

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SLIDE 65

ACCELERATED CORROSION TESTING OF PANI COATINGS ON STEEL :

  • 0.5
  • 0.3
  • 0.1

0.1 0.3 0.5 0.7 3 6 9 12 15

Number of Days OCP / V

(a) (b) (c) (d)

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SLIDE 66

PCB Type FC stack INTER CONNECTS FOR PLANAR FC

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SLIDE 67

Typical Thin Plates Reported for DMFC :

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SLIDE 68

Floppy for comparison Internal stack Fuel Cells : As thin as you can get !!

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SLIDE 69

PERFORMANCE OF THIN PCB TYPE FC

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SLIDE 70

Portable fuel cells using very thin configuration : screen printing technology Toshiba announced the DMFC for Laptops MTI Micro fuel cells- DMFC for Cell phone (Samsung) Mini and Micro fuel cells require very thin electrodes and bipolar connects

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SLIDE 71

ADVANTAGES OF NEW MATERIALS AND TECHNIQUES FOR BIPOLAR PLATES

  • LARGE SCALE PRODUCTION POSSIBLE LEADING TO

LOW COST

  • HIGH TEMPERATURE (>500C ) PROCESSING NOT

REQUIRED

  • LOW WASTAGE OF MATERIALS
  • CONTACT RESISTANCE IS REDUCED (Graphite based

plates have problems due to bolts tightening limits)

  • MORE FLEXIBILITY FOR DESIGN
  • WIDER RANGE OF MATERIALS CAN BE MADE AVAILABLE
  • NEW HYBRID MATERIALS WITH MULTIPLE

FUNCTIONALITY CAN BE TRIED

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SLIDE 72