Portable LPG-Fueled Microtubular Fuel Cell

Portable LPG-Fueled Microtubular Fuel Cell Dr. Sascha Kühn Hannover Messe 2013, Technical Forum, Hannover 10th of April 2013 Funded by the European Un...
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Portable LPG-Fueled Microtubular Fuel Cell Dr. Sascha Kühn Hannover Messe 2013, Technical Forum, Hannover 10th of April 2013 Funded by the European Union and the Free State of Saxony

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Markets

Comparison

Portable and Mobile Applications

weight per time

Leistungsanforderung

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APU range extender UAV

1000 W

LTEFunk

LEV Scooter

500 W

Emergency Power

Boats Cargobike

E-Bikes GSMFunk

Emergency -Kit

Camping Leisure

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mobil

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Mobilitätsgrad

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Energy storage

Mobile Markets 2017

Comparison

Power density, robustness, quick-start

Power Density (W/kg)

50 W, soldier power

Values based on: Pike Research Study, 2012

go::batt 375

attractivity

500 W, UAV go::batt 5000

200 W, millitary power

200 W, emergency power

go::batt 125

1 W, models

go::batt 5

Energy Density (Wh/kg)

50 W, emergency power

3.000 W, emergency power

500 W, emergency power

1 W, personal power

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USPs

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eZelleron GmbH The Company

- We can use available fuels (LPG) not only hydrogen - quick-startable for mobile applications - Extremely light-weight due to high power density - Cost efficient (materials choice, mass manufacturing methods)

Founded 12/2007, 22 Employees Strategic Partners: Upper Austria University (2 Project Staff) Fraunhofer IKTS (22 Project Staff) IP Big Portfolio of 13 worldwide Patent Familys (USA, Japan, Europe) Several receips, strategic documents and publications

Hall 27 B50

Pre-Seed-Capital: > 10 Mio. EUR Seed-Capital: 3,1 Mio. EUR Funded Project Volume: 7,5 Mio. EUR

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Outline

Fuel Cell – Technological Issues Power Density, Robustness, Quick-startability O2-

Cermet Anode Substrate  Why Powder Injection Moulding?  Mass-Manufacturing of Substrates  Proprietary Binder System

eO2

Thin film technology for the Electrolyte Layer  Electrophoretic Deposition (EPD)  Stacking  System

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Ceramic Processing Methods

O2H+

ee-

O2-H

O2-

e-

Cathode  polarisation resistance  (ohmic, concentration)  activation energy  reaction area

O2

Electrolyte

H2

 oxygen vacancy formation enthalpy

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Rough summary

ionic cond. metallic cond.

 materials, temperature  microstructure (TPB, percolation)  internal ionic resistance

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ionic cond. mixed cond.

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+

H++ eeH

H2

Anode  polarisation resistance (ohmic, concentration)  activation energy  reaction area  electric conductivity  materials, temperature  particle size distr.  microstructure (TPB, percolation)

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Binder system & Feedstock high requirements on accuracy

Material preparation/ Compounding

Complexity of the workpiece

Identification of suitable combinations of organic Adjuvants -

Uniaxial pressing

Hot Moulding

Wetting agents Disperser Plastisicer Binder Release agents Defoamer

Cold isostatic pressing

Mechanic, chemical und thermomechanic process engineering

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Debindering Technologies Thermal

Solvent (eZelleron)

• quick • very quick • nearly no emissions • no emissions • binder recycling • lowest cost

Advantages Disadvantages

Katalytic

Bindersystem & Feedstock

• long process times • impossible for complex geometries • high poluting emissions

• dangerous reactants

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Material

Parameters

Density Binder

~0,9 g/cm3

Density Feedstock

~3 g/cm3

Powder Content

~80 gew-%

Processing Temperature

130-145 °C (SG)

Tool Temperture

~50 °C

Processing of Feedstocks

Debindering

Injection Pressure about 200 bar

Solution Debindering

Relative high Viskosity

Temperature: 60°C

High Green Density Good Demoulding Capacities

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Cycle Times: 4 – 6 h Backbone Debindering at 1000°C

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Powder Injection Moulding

Scheer Extruder

Parameters

• • • •

Gap width Temperatures Roller speed Feeding speed • • • • • • •

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viscosity speed temperatures (Tool, nozzle, cooling) pressure, after pressure geometries (nozzle, screw) clamping force materials (abrasion resistance)

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Injection Moulding

Injection Moulding

Computertomography

Influence of CIM-Parameters

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Gasdiffusion

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Outline

Mercury-Porosimetry of Ni-Samples

4,0 3,0 2,0 1,0

50 47 % useable Porevolume

40 30 20

Cumulated specific Porevolume (%TD)

medium free waylenght H2, 700 °C

Relative Porevolume (%)

5,0

Cermet Anode Substrate  Why Powder Injection Moulding?  Mass-Manufacturing of Substrates  Proprietary Binder System Thin film technology for the Electrolyte Layer  Electrophoretic Deposition (EPD)  Stacking  System

10

0,0

System development  Stacking  Hotbox  System

0 1

10

100

1000

10000

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Fuel Cell – Technological Issues

How to reach the Goal?

Power Density, Robustness, Quick-startability

O2

eee-

O2

Electrolyte

H2

 materials, temperature  microstructure (TPB, percolation)  internal ionic resistance  oxygen vacancy formation enthalpy eZelleron GmbH - Copying prohibited!

O2H+ + O2-H

O2-

Cathode  polarisation resistance  (ohmic, concentration)  activation energy  reaction area

process development for the electrolyte

ionic cond. metallic cond.

H++ H

ee-

H2

Requirements

Goal

 Power Density  Robustness  Quick-startability

 Materials, temperature  Thermomech. Stability  High ionic conductivity

Anode  polarisation resistance (ohmic, concentration)  activation energy  reaction area  electric conductivity

 Thin layer (no weibull behaviour, low resistance)  Low grain size (mechanical stability, conductivity)  Good adhesion (thermomechanical)  Nanopowders  Low sintering temperatures (high green densitys)  Impregnation

 materials, temperature  particle size distr.  microstructure (TPB, percolation)

 Electrophoretic Impregnation  Electrophoretic Deposition

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Crystallite Size 27 nm

Electric current (A)

40 nm

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Correlation of Layer Thickness

YSZ: Habitus of the powder

Particle Size

Issues  internal ionic resistance  oxygen vacancy formation enthalpy

0,8

80

0,7

70

0,6

60

0,5

50

0,4

40

0,3

30

0,2

20

0,1

0,1 µm.

10

1150 °C, Basis, 24 V

0 0

20

40

60

80

100

Layer Thickness (µm)

O2e-

ionic cond. mixed cond.

0 120

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Impregnated membrane 0 µm

70 µm

1 µm.

Green layer 100 µm

1 µm.

180 µm

1 µm.

1 µm.

5 µm.

30 µm.

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Resulting microstructure

Advanced Microstructure

EPD, sintered at 1250 °C

SEM

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1 µm.

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Microtubular Fuel Cells

Aufbau der eZelleron SOFC

Sintering – Mass-production

Prozessschritte

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Advantage: High Power-Density

Long term test

2008 Cell Generation (LSCF-Cathode)

750 h Test

• high power-densities • no up-scaling just numbering up • quick development cycles

1600 1400

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active area: 3,7 cm² Fuel: 98 % H2, 2 % H2O, FU: 60 % Oxidant: Air, AU: 15 %

1200

P (mW/cm²)

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1000

P (mW/cm²) @ 0,7 V

800 600

active area: 3,7 cm² Fuel: 98 % H2, 2 % H2O, FU: 60 % Oxidant: Air, AU: 15 % Voltage: 0,7 V

400 200

One tube has 3,7 cm², that means > 5 W @ 850 °C

0 600

650

700

750

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800

850

900

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Massproduction of Microtubues

Outline

Any quantity available.

• • • • •

Cermet Anode Substrate  Why Powder Injection Moulding?  Mass-Manufacturing of Substrates  Proprietary Binder System

cheap compact (47 x 3 mm / 1,7 g) robust und quick-startable Very good cycleable Fueled by LPG (Propane/ Butane)

Thin film technology for the Electrolyte Layer  Electrophoretic Deposition (EPD)  Stacking  System

System development  Stacking  Hotbox  System 25.03.2013

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Stack

Cell in Stack Environment

go::batt 125

Power losses 1,2

1,0

Voltage (V)

2,0

850 °C 800 °C 750 °C

1,8 1,6 1,4

0,8

1,2

0,6

1,0 0,8

0,4

0,6

0,2

0,4

active area: 3,7 cm² Fuel: 98 % H2, 2 % H2O, FU: 60 % Oxidant: Air, AU: 15 %

0,2

0,0

0,0 0,00

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electrical power(W)

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0,50

1,00

1,50

2,00

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2,50

3,00 www.eZelleron.de

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Cell in Stack Environment

Cell in Stack Environment

Fuel Utilisation 3,50

Thermocycling Capability

2,50

electrical power(mW/cm²)

3,00

Current (A)

600

0,6 V 0,7 V 0,8 V

2,00 1,50 1,00 0,50 0,00 0%

20%

40%

60%

80%

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400 300 200 100 0

100%

0

Fuel Utilisation FU eZelleron GmbH - Copying prohibited!

500

200

400

600

800

1000

cycle Nr. www.eZelleron.de

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Stack

Stack

250 h -Test

Fully Automated Thermal Cycling

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14 12 10

P (W)

8 6 4

Temp.: 850 °C Fuel: synth. Reformat Oxidant: Air, AU: 15 % Voltage: 0,7 V

2 0

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Hotbox

Gasbattery

Fully integrated system

go::batt 125

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Gasbatteries

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Come to our Booth

eZell2

LPG - worldwide available! No precious metals! Up to 20 times lighter than Li-Ion-Batteries.

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Stack

Lightweight design 850 W, 1,7 kg 360 tubes, 2 g per tube 240,0

850 °C 800 °C 750 °C

20,0

200,0

12,0

120,0

8,0

80,0

4,0

40,0

Voltage (V)

160,0

0,0 0,00

5,00

10,00

15,00

70 mm

16,0

electrical power(W)

24,0

0,0 20,00

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AR-200 AirCell

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Comparison PEM, SOFC, eZelleron Feature

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PEM

SOFC eZell

Efficiency above 50 % possible





Operates on Hydrocarbons (LPG,…)





No Water Management needed (OT > 100 °C)





No Outside and Storage Temp. Limitation





Easy Fuel Processing





Easy System Architecture





Useable Waste Heat Temp.





No Noble Metalls needed (Price)





Power density above 0,3 kW/kg





Very good ruggedness (vibrations, …)





Start-up time below 1 Minute





More than 100 Cycles





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eZelleron

Cooperate with us!

Conclusion

• • • • • •

Feedstocks (mass production) Cells (mass Production) Stacks (small series production, customer made solutions) Hotbox (customer made solutions in the end of 2013) Gasbatteries (available in 2014 + customer made solutions) Individual hybrid systems (customer made solutions) Dr.-Ing. Sascha Kühn Managing Director / CTO

eZelleron GmbH Winterbergstr. 28 01277 Dresden · Germany tel.: +49 351 250 88 78 - 0 mob.: +49 176 13 93 55 - 10 fax: +49 351 250 88 78 - 9 [email protected] eZelleron GmbH - Copying prohibited!

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Funded by the European Union and the Free State of Saxony

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Copyright 2008-2011 eZelleron GmbH Alle Rechte vorbehalten



• • • •



Weitergabe und Vervielfältigung dieser Publikation oder von Teilen daraus sind, zu welchem Zweck und in welcher Form auch immer, ohne die ausdrückliche schriftliche Genehmigung durch die eZelleron GmbH nicht gestattet. In dieser Publikation enthaltene Informationen können ohne vorherige Ankündigung geändert werden. Die von der eZelleron GmbH oder deren Vertriebsfirmen angebotenen Produkte können Komponenten anderer Hersteller enthalten. iPhone und iPad sind Marken der Apple Inc. (Cupertino, Kalifornien, USA) SEGWAY ist eine Marke der Segway Inc. (Bedford, New Hampshire, USA) eZelleron, go::batt 5, go::batt 125, go::batt 375 und weitere im Text erwähnte eZelleron-Produkte und -Dienstleistungen sowie die entsprechenden Logos sind Marken oder eingetragene Marken der eZelleron GmbH in Deutschland und anderen Ländern weltweit. Alle anderen Namen von Produkten und Dienstleistungen sind Marken der jeweiligen Firmen

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