metal hydride storage tank - ele.energy.dtu.dk

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Metal Hydride Storage Tank J. O Jensen 1,* , E. Hennesø 1 , Q. Li 1 , J. J. Bentzen 2 , A. S. Pedersen 2 , S. Yde-Andersen 3 and N. J. Bjerrum 1 1 Department of Chemistry, Technical University of Denmark, Kemitorvet 207, DK-2800 Kgs. Lyngby, Denmark 2 Risø DTU, Materials Research Department, AFM-228, Technical University of Denmark, DK-4000 Roskilde, Denmark 3 IRD Fuel Cells A/S, Kullinggade 31, DK-5700 Svendborg, Denmark * E-mail: [email protected] Abstract A hydrogen storage tank was developed and constructed based on metal hydride powder contained in aluminium compartments. The aim was to develop a tank for a hydrogen powered car with a water cooled internal combustion engine (ICE). A model tank with an internal volume of about one litre was fitted with a heat exchanger and metal hydride alloy powder of the AB 5 type from GfE (Germany). Charging time (95%) was about 20 min. with tap water cooling and discharging time (95%) about 30 min. using 85-90ºC water as the heat source. Later the tank was up-scaled, but changed geometrical requirements from the end-user led to a re-dimensioning of the heat exchanger. As a consequence the rates for charging and discharging became somewhat lower. JOJ June 2008 First tank (vol ~1L) Third tank (vol 17,5L) Second tank (vol ~1L) Acknowledgement: The authors which to acknowledge the Danish Energy Authority, the Hydrogen Programme. For financial support of the work. The improved heat exchanger in Tank 2 after testing. The aluminium compartment served two purposes; 1) as heat conductors and 2) to prevent compaction of the powder. The central tube for water cannot be seen. No visible damage was detected. Left: Tank 1 during testing. Right: The copper plate heat exchanger after a number of charge discharge cycles. Note it is severely bent due to the expansion forces of the powder. Left: Charging of tank 2. Cooling by tap water. Right: Discharging. Heating by 85-90ºC water (attempted cooling water from vehicular ICE) 0,00 0,20 0,40 0,60 0,80 1,00 1,20 1,40 1,60 1,80 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 Cycle no. Hydrogen (w%) 0 20 40 60 80 100 Time for 95 % (min) 0,00 0,20 0,40 0,60 0,80 1,00 1,20 1,40 1,60 1,80 0 1 2 3 4 5 6 7 8 9 10 11 Cycle no. Hydrogen (w%) 0 10 20 30 40 50 60 70 80 90 100 Time for 95 % (min) 0 10 20 30 40 50 60 70 80 90 100 0,0 0,5 1,0 Time (hours) Temperature ( o C), and Pressure (bar (o)) 0 50 100 150 200 250 300 350 400 450 500 Hydrogen (NL), and Heat (kcal) Pressure Litre H 2 Temp. water out Removed heat Charge 0 10 20 30 40 50 60 70 80 90 100 0,0 0,5 1,0 Time (hours) Temperature ( o C), and Pressure (bar (o)) 0 50 100 150 200 250 300 350 400 450 500 Hydrogen (NL), and Heat (kcal) Temp. Water out Heat supplied Litre H 2 Pressure Discharge For submission to: Int. J. Hydrogen Energy Left: The result of 10 charge/discharge 10 cycles of tank 2 with pure hydrogen (99.9999%). Filled markers: filling, open markers: discharge. Time for 95% completion. Right: 10 more cycles with technical quality hydrogen. (low purity ) Left: Cross section of final tank. Mid: The final tank. Volume 17.5 L. 29 kg hydride. Right: one compartment during filling (in air)

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Page 1: Metal Hydride Storage Tank - ele.energy.dtu.dk

Metal Hydride Storage Tank

J. O Jensen1,*, E. Hennesø1, Q. Li1, J. J. Bentzen2, A. S. Pedersen2, S. Yde-Andersen3 and N. J. Bjerrum1

1Department of Chemistry, Technical University of Denmark, Kemitorvet 207, DK-2800 Kgs. Lyngby, Denmark

2Risø DTU, Materials Research Department, AFM-228, Technical University of Denmark, DK-4000 Roskilde, Denmark 3IRD Fuel Cells A/S, Kullinggade 31, DK-5700 Svendborg, Denmark

*E-mail: [email protected]

Abstract A hydrogen storage tank was developed and constructed based on metal hydride powder contained in aluminium compartments. The aim was to develop a tank for a hydrogen powered car with a water cooled internal combustion engine (ICE). A model tank with an internal volume of about one litre was fitted with a heat exchanger and metal hydride alloy powder of the AB5 type from GfE (Germany). Charging time (95%) was about 20 min. with tap water cooling and discharging time (95%) about 30 min. using 85-90ºC water as the heat source. Later the tank was up-scaled, but changed geometrical requirements from the end-user led to a re-dimensioning of the heat exchanger. As a consequence the rates for charging and discharging became somewhat lower.

JOJ June 2008

First tank (vol ~1L)

Third tank (vol 17,5L)

Second tank (vol ~1L)

Acknowledgement: The authors which to acknowledge the Danish Energy Authority, the Hydrogen Programme. For financial support of the work.

The improved heat exchanger in Tank 2 after testing. The aluminium compartment served two purposes; 1) as heat conductors and 2) to prevent compaction of the powder. The central tube for water cannot be seen. No visible damage was detected.

Left: Tank 1 during testing.

Right: The copper plate heat exchanger after a

number of charge discharge cycles. Note it

is severely bent due to the expansion forces of

the powder.

Left: Charging of tank 2. Cooling by tap water.

Right: Discharging. Heating by 85-90ºC water (attempted

cooling water from vehicular ICE)

0,000,200,400,600,801,001,201,401,601,80

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16

Cycle no.

Hyd

roge

n (w

%)

0

20

40

60

80

100

Tim

e fo

r 95

% (m

in)

0,000,200,400,600,801,001,201,401,601,80

0 1 2 3 4 5 6 7 8 9 10 11

Cycle no.

Hyd

roge

n (w

%)

0102030405060708090100

Tim

e fo

r 95

% (m

in)

0

10

20

30

40

50

60

70

80

90

100

0,0 0,5 1,0

Time (hours)

Tem

pera

ture

(o C),

and

Pres

sure

(bar

(o))

0

50

100

150

200

250

300

350

400

450

500

Hyd

roge

n (N

L),

and

Hea

t (kc

al)

Pressure

Litre H2

Temp. water out

Removed heat

Charge

0

10

20

30

40

50

60

70

80

90

100

0,0 0,5 1,0

Time (hours)

Tem

pera

ture

(o C),

and

Pres

sure

(bar

(o))

0

50

100

150

200

250

300

350

400

450

500

Hyd

roge

n (N

L),

and

Hea

t (kc

al)

Temp. Water out

Heat supplied

Litre H2

Pressure

Discharge

For submission to:

Int. J. Hydrogen Energy

Left: The result of 10 charge/discharge 10 cycles of tank 2 with pure hydrogen (99.9999%). Filled markers: filling, open markers: discharge. Time for 95% completion.

Right: 10 more cycles with technical quality hydrogen.

(low purity )

Left: Cross section of final tank. Mid: The final tank. Volume 17.5 L. 29 kg hydride. Right: one compartment during filling (in air)