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Optimization of AB2 - type alloy composition with superior
hydrogen storage properties for stationary applications
Kandavel Manickam, David Grant and Gavin Walker
Energy and Sustainability Research Division
Faculty of Engineering
The University of Nottingham

ICAER 2013, IIT Bombay
Outline

1. Introduction
2. Results of AB2 type alloys
•
•
•
•
•

Materials preparation and characterization
P-C-I measurements
Thermodynamics
Hydrogenation kinetics
HP-DSC studies of alloys

3. Summary of results and conclusions
Introduction

Year

Limited reserves

CO2

Global warming

Alternative clean energies
Hydrogen can be a clean energy carrier
• High energy density (three time higher than the fossil fuels)
• Environmental friendliness (H2O)

Hydrogen economy
• Production
• Storage
• Utilization
BioCPV
• Indo – UK BURD (Bridging the Urban and Rural Divide) Project
• Integration of different types of energy sources and energy storage technologies

12 kWh

16 kWh

14 kWh

H store

End user

Electrolyser

7.5 kWh

2520 litres
CPV- 15 kWp
120 kWh per day

Hydrogen
7 kWh

2350 litres

Bio waste
22 kWh
14000 litres

Bio gas plant (14 m3)

Genset

Village electrification

90 kWh
Materials selection requirements
Hydrogen storage
• 7.5 kWh(H2) : 225 g H2
• equivalent to 2520 litres (stp)
• Solid State Storage
• 15 kg AB alloy (1.6 wt %)
• 13 kg of AB2 alloy (1.8 wt %)

Commercial Hydralloy C - AB2 alloy
• Plateau Pressure : 13 bar
• Capacity : 1.3 wt %

Aim of the present work

Requirements

1 g H2/min

Kinetics

• AB2 type Laves phase alloys
• Composition variation to improve
hydrogen storage properties
• Effect of non-stoichiometry on the
hydrogen storage properties
• Identification of suitable composition
for the BioCPV application
Synthesis & Characterization
172.0

A1+xB2(x = 0, 0.05, 0.075 and 0.1)
40

50

60

70
3

Unitcell volume (Å )

30

A1+xB2
171.5

x = 0.1

x = 0.075

171.0
170.5
170.0
169.5

Intensity (arb. units)

169.0

0.00

0.04

0.08

0.12

x in A1+xB2

x=0

x = 0.05

x = 0.075

x = 0.1

30

40

(201)

50

2

60

• Single phase formation
• Hexagonal structure (C14)
• space group P63/mmc

(205)

(302)

(104)

(213)

x=0
(202)

(004)

(112)
(200)

(103)

(110)

x = 0.05

70

Composition is similar to initial composition (± 1%)
Hydrogen storage
Pressure – Composition Isotherms

Equilibirum Pressure (bar)

100

α phase

2.1 wt %

A1.05B2

10

β
α+β

1

Plateau pressure
o

32 C
o
50 C
o
60 C
o
70 C

0.1

α

0.01
0.0

0.4

0.8

1.2

1.6

Hydrogen concentration (wt %)

α+β phase

2.0

β phase
Pressure – Composition Isotherms
A1.05B2

100

100

Equilibirum Pressure (bar)

Hydrogenation

Dehydrogenation

15 bar

10

10

1

1

0.01
0.0

1.55 wt %

o

32 C
o
50 C
o
60 C
o
70 C

0.1

0.4

0.8

1.2

1.6

1 bar

o

32 C
o
50 C
o
60 C
o
70 C
2.0 0.0

0.4

0.8

1.2

1.6

Hydrogen concentration (wt %)

Working capacity (1 to 15 bar) at 32 oC ~ 1.55 wt %

2.0

0.1

0.01
100
A1+xB2

Increase in storage capacity
• Modification of chemical
environment of interstitial
sites
• Size of the interstitial sites

10

1

o

T = 32 C
0.4

0.8

1.2

1.6

Hydrogen Concentration (wt %)

2.0

0.00
2.4
2.0

0.05

0.10

Storage capacity
Working capacity
Plateau pressure

20

Plateau pressure (bar)

x=0
x = 0.05
x = 0.075
x = 0.1

0.1

0.01
0.0

Rietveld analysis and neutron
diffraction

Hydrogen concentartion (wt %)

Equilibrium Pressure (bar)

Pressure – Composition Isotherms

16

1.6

12

1.2

8

0.8

4

0.4

0.00

0.05

x in A1+xB2

0.10

0
Thermodynamics
van’t Hoff relation :

𝑙𝑛𝑃 𝐻2 =

Hydrogenation

∆𝐻
∆𝑆
−
𝑅𝑇
𝑅

Dehydrogenation

2.4

2.4

ln PH2

ln PH2

1.6

1.6
0.8

0.8

0.0028

x = 0.05
x = 0.075
x = 0.1

x = 0.05
x = 0.075
x = 0.1

0.0030

0.0032

Hydrogenation
ΔH = - 25 to -28 kJ/mol H2
ΔS = - 92 to -100 J/K/mol H2

0.0028
0.0034

0.0030

0.0032

0.0
0.0034

1/T (1/K)

Dehydrogenation
ΔH = 28 to 32 kJ/mol H2
ΔS = 94 to 112 J/K/mol H2
Hydrogenation Kinetics
Avrami-Erofeev rate eq: F = 1- exp(-ktn); n = 0.54 to 3

2.0

6

First order rate equation : - ln(1-F) = kt

5
4

1.5

- ln (1-F)

Hydrogen Concentration (wt %)

Working Capacity

o

A1.05B2

1.0

0
0.0

32 C
o
50 C
o
60 C
o
70 C

20

60

40

80

3
2

100

0

A1.05B2
0

20

60

Time (min)

80

100

β phase
ln D vs 1/T

-29.4

-0.7

-1.4

Ea : 24 ± 1 kJ/mol
0.0030

0.0032

1/T (1/K)

0.0034

2

π 𝐷
𝑟2

r = 5 μm
Arrhenius relation
D = D0 exp(-Ea/kbT)

ln D

ln k

kd=

0.0028

40

Arrhenius relation
k = k0 exp(-Ea/kbT)

lnk vs 1/T

o

32 C
o
50 C
o
60 C
o
70 C

α+β

1

Time (min)

α+β phase

β

-30.0

-30.6
0.0028

Ea : 29 ± 1 kJ/mol
0.0030

0.0032

1/T (1/K)

0.0034
Hydrogen gas
Heating rate = 5 oC/min
Flow rate = 100 ml/min

van’t Hoff relation : 𝑙𝑛𝑃 𝐻2 =

∆𝐻
∆𝑆
−
𝑅𝑇
𝑅

Validation of PCI measurements

0.2
20 bar
16 bar
12 bar
8 bar

A1.05B2
0.1

2.8

Dehydrogenation
ln PH2

DSC Heat flow (mW/mg)

High Pressure DSC

0.0

2.1

Hydrogenation
-0.1
1.4

50

100

150

200

250

Hydrogenation
Dehydrogenation

A1.05B2
0.0026

o

0.0028

0.0030

1/T (1/K)

Temperature ( C)

A2B2 Interstitial sites: 24l, 12k, 6h1, 6h2
Low temperature peak : 24l and 6h1
High temperature peak : 12k and 6h2

Hydrogenation
ΔH = - 29 ± 2 kJ/mol H2
ΔS = - 100 ± 4 J/K/mol H2

Dehydrogenation
ΔH = 32 ± 4 kJ/mol H2
ΔS = 117 ± 9 J/K/mol H2
Summary of results
PCI measurements

DSC measurements

Plateau slope
factor
ln(P2/P1)

ΔH

ΔS

ΔH

ΔS

(kJ/mol H2)

(J/K/mol H2)

(kJ/mol H2)

(J/K/mol H2)

Alloy 1 (x = 0)

2.7

-

-

- 29 ± 2

- 100 ± 5

Alloy 2 (x = 0.05)

2.4

- 26 ± 2

- 98 ± 5

- 29 ± 2

- 100 ± 4

Alloy 3 (x = 0.075)

2.2

- 25 ± 1

- 92 ± 3

-26 ± 3

- 96 ± 8

Alloy 4 (x = 0.1)

1.9

- 28 ± 1

- 100 ± 2

- 28 ± 1

- 99 ± 1

Alloy
Summary of results

Alloy

Plateau
pressure
(bar)

Storage
capacity
at 15 bar

Residual
storage
capacity
(1 bar)

Working
capacity
(15 to 1
bar)

Charge
time : 95
%
(min)

1.7

32 oC 50 oC

Max.
Storage
capacity
(wt%)
@ ~ 35 bar

1.6

0.3

1.3

6

Alloy 1 (x = 0)

6.0
3.2

Alloy 2 (x = 0.05)

5.3
2.8

8.2
5.6

2.1

1.85

0.3

1.55

5

Alloy 3 (x = 0.075)

3.0
1.7

5.4
3.5

2.1

2.0

0.55

1.45

5

Alloy 4 (x = 0.1)

2.2
1.4

4.1
2.4

2.2

2.1

0.7

1.4

5
Conclusions

Single phase non-stoichiometric AB2 Laves phase alloys have
synthesized successfully

Alloy 2 (x = 0.05) is most promising for the BioCPV application

Working capacity reached within 5 min at 32 °C

16 % increase in
storage capacity
than Hydralloy C

Interstitial sites can be
modified by preparing
non stoichiometric
alloys
Thank you
Manickam.Kandavel@nottingham.ac.uk
David.Grant@nottingham.ac.uk
Gavin.Walker@nottingham.ac.uk

Acknowledgement
- Research group members

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329 Kandavel

  • 1. Optimization of AB2 - type alloy composition with superior hydrogen storage properties for stationary applications Kandavel Manickam, David Grant and Gavin Walker Energy and Sustainability Research Division Faculty of Engineering The University of Nottingham ICAER 2013, IIT Bombay
  • 2. Outline 1. Introduction 2. Results of AB2 type alloys • • • • • Materials preparation and characterization P-C-I measurements Thermodynamics Hydrogenation kinetics HP-DSC studies of alloys 3. Summary of results and conclusions
  • 3. Introduction Year Limited reserves CO2 Global warming Alternative clean energies Hydrogen can be a clean energy carrier • High energy density (three time higher than the fossil fuels) • Environmental friendliness (H2O) Hydrogen economy • Production • Storage • Utilization
  • 4. BioCPV • Indo – UK BURD (Bridging the Urban and Rural Divide) Project • Integration of different types of energy sources and energy storage technologies 12 kWh 16 kWh 14 kWh H store End user Electrolyser 7.5 kWh 2520 litres CPV- 15 kWp 120 kWh per day Hydrogen 7 kWh 2350 litres Bio waste 22 kWh 14000 litres Bio gas plant (14 m3) Genset Village electrification 90 kWh
  • 5. Materials selection requirements Hydrogen storage • 7.5 kWh(H2) : 225 g H2 • equivalent to 2520 litres (stp) • Solid State Storage • 15 kg AB alloy (1.6 wt %) • 13 kg of AB2 alloy (1.8 wt %) Commercial Hydralloy C - AB2 alloy • Plateau Pressure : 13 bar • Capacity : 1.3 wt % Aim of the present work Requirements 1 g H2/min Kinetics • AB2 type Laves phase alloys • Composition variation to improve hydrogen storage properties • Effect of non-stoichiometry on the hydrogen storage properties • Identification of suitable composition for the BioCPV application
  • 6. Synthesis & Characterization 172.0 A1+xB2(x = 0, 0.05, 0.075 and 0.1) 40 50 60 70 3 Unitcell volume (Å ) 30 A1+xB2 171.5 x = 0.1 x = 0.075 171.0 170.5 170.0 169.5 Intensity (arb. units) 169.0 0.00 0.04 0.08 0.12 x in A1+xB2 x=0 x = 0.05 x = 0.075 x = 0.1 30 40 (201) 50 2 60 • Single phase formation • Hexagonal structure (C14) • space group P63/mmc (205) (302) (104) (213) x=0 (202) (004) (112) (200) (103) (110) x = 0.05 70 Composition is similar to initial composition (± 1%)
  • 7. Hydrogen storage Pressure – Composition Isotherms Equilibirum Pressure (bar) 100 α phase 2.1 wt % A1.05B2 10 β α+β 1 Plateau pressure o 32 C o 50 C o 60 C o 70 C 0.1 α 0.01 0.0 0.4 0.8 1.2 1.6 Hydrogen concentration (wt %) α+β phase 2.0 β phase
  • 8. Pressure – Composition Isotherms A1.05B2 100 100 Equilibirum Pressure (bar) Hydrogenation Dehydrogenation 15 bar 10 10 1 1 0.01 0.0 1.55 wt % o 32 C o 50 C o 60 C o 70 C 0.1 0.4 0.8 1.2 1.6 1 bar o 32 C o 50 C o 60 C o 70 C 2.0 0.0 0.4 0.8 1.2 1.6 Hydrogen concentration (wt %) Working capacity (1 to 15 bar) at 32 oC ~ 1.55 wt % 2.0 0.1 0.01
  • 9. 100 A1+xB2 Increase in storage capacity • Modification of chemical environment of interstitial sites • Size of the interstitial sites 10 1 o T = 32 C 0.4 0.8 1.2 1.6 Hydrogen Concentration (wt %) 2.0 0.00 2.4 2.0 0.05 0.10 Storage capacity Working capacity Plateau pressure 20 Plateau pressure (bar) x=0 x = 0.05 x = 0.075 x = 0.1 0.1 0.01 0.0 Rietveld analysis and neutron diffraction Hydrogen concentartion (wt %) Equilibrium Pressure (bar) Pressure – Composition Isotherms 16 1.6 12 1.2 8 0.8 4 0.4 0.00 0.05 x in A1+xB2 0.10 0
  • 10. Thermodynamics van’t Hoff relation : 𝑙𝑛𝑃 𝐻2 = Hydrogenation ∆𝐻 ∆𝑆 − 𝑅𝑇 𝑅 Dehydrogenation 2.4 2.4 ln PH2 ln PH2 1.6 1.6 0.8 0.8 0.0028 x = 0.05 x = 0.075 x = 0.1 x = 0.05 x = 0.075 x = 0.1 0.0030 0.0032 Hydrogenation ΔH = - 25 to -28 kJ/mol H2 ΔS = - 92 to -100 J/K/mol H2 0.0028 0.0034 0.0030 0.0032 0.0 0.0034 1/T (1/K) Dehydrogenation ΔH = 28 to 32 kJ/mol H2 ΔS = 94 to 112 J/K/mol H2
  • 11. Hydrogenation Kinetics Avrami-Erofeev rate eq: F = 1- exp(-ktn); n = 0.54 to 3 2.0 6 First order rate equation : - ln(1-F) = kt 5 4 1.5 - ln (1-F) Hydrogen Concentration (wt %) Working Capacity o A1.05B2 1.0 0 0.0 32 C o 50 C o 60 C o 70 C 20 60 40 80 3 2 100 0 A1.05B2 0 20 60 Time (min) 80 100 β phase ln D vs 1/T -29.4 -0.7 -1.4 Ea : 24 ± 1 kJ/mol 0.0030 0.0032 1/T (1/K) 0.0034 2 π 𝐷 𝑟2 r = 5 μm Arrhenius relation D = D0 exp(-Ea/kbT) ln D ln k kd= 0.0028 40 Arrhenius relation k = k0 exp(-Ea/kbT) lnk vs 1/T o 32 C o 50 C o 60 C o 70 C α+β 1 Time (min) α+β phase β -30.0 -30.6 0.0028 Ea : 29 ± 1 kJ/mol 0.0030 0.0032 1/T (1/K) 0.0034
  • 12. Hydrogen gas Heating rate = 5 oC/min Flow rate = 100 ml/min van’t Hoff relation : 𝑙𝑛𝑃 𝐻2 = ∆𝐻 ∆𝑆 − 𝑅𝑇 𝑅 Validation of PCI measurements 0.2 20 bar 16 bar 12 bar 8 bar A1.05B2 0.1 2.8 Dehydrogenation ln PH2 DSC Heat flow (mW/mg) High Pressure DSC 0.0 2.1 Hydrogenation -0.1 1.4 50 100 150 200 250 Hydrogenation Dehydrogenation A1.05B2 0.0026 o 0.0028 0.0030 1/T (1/K) Temperature ( C) A2B2 Interstitial sites: 24l, 12k, 6h1, 6h2 Low temperature peak : 24l and 6h1 High temperature peak : 12k and 6h2 Hydrogenation ΔH = - 29 ± 2 kJ/mol H2 ΔS = - 100 ± 4 J/K/mol H2 Dehydrogenation ΔH = 32 ± 4 kJ/mol H2 ΔS = 117 ± 9 J/K/mol H2
  • 13. Summary of results PCI measurements DSC measurements Plateau slope factor ln(P2/P1) ΔH ΔS ΔH ΔS (kJ/mol H2) (J/K/mol H2) (kJ/mol H2) (J/K/mol H2) Alloy 1 (x = 0) 2.7 - - - 29 ± 2 - 100 ± 5 Alloy 2 (x = 0.05) 2.4 - 26 ± 2 - 98 ± 5 - 29 ± 2 - 100 ± 4 Alloy 3 (x = 0.075) 2.2 - 25 ± 1 - 92 ± 3 -26 ± 3 - 96 ± 8 Alloy 4 (x = 0.1) 1.9 - 28 ± 1 - 100 ± 2 - 28 ± 1 - 99 ± 1 Alloy
  • 14. Summary of results Alloy Plateau pressure (bar) Storage capacity at 15 bar Residual storage capacity (1 bar) Working capacity (15 to 1 bar) Charge time : 95 % (min) 1.7 32 oC 50 oC Max. Storage capacity (wt%) @ ~ 35 bar 1.6 0.3 1.3 6 Alloy 1 (x = 0) 6.0 3.2 Alloy 2 (x = 0.05) 5.3 2.8 8.2 5.6 2.1 1.85 0.3 1.55 5 Alloy 3 (x = 0.075) 3.0 1.7 5.4 3.5 2.1 2.0 0.55 1.45 5 Alloy 4 (x = 0.1) 2.2 1.4 4.1 2.4 2.2 2.1 0.7 1.4 5
  • 15. Conclusions Single phase non-stoichiometric AB2 Laves phase alloys have synthesized successfully Alloy 2 (x = 0.05) is most promising for the BioCPV application Working capacity reached within 5 min at 32 °C 16 % increase in storage capacity than Hydralloy C Interstitial sites can be modified by preparing non stoichiometric alloys