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Approach:<br />

An off-board regenerable liquid carrier <strong>for</strong><br />

vehicles and stationary H 2<br />

gas delivery<br />

LQ*H 2<br />

LQ = liquid carrier<br />

∆ = heat<br />

Liquid<br />

Storage Tank<br />

LQ<br />

Catalytic<br />

Converter<br />

∆<br />

Heat Exchange<br />

∆<br />

Fuel Cell<br />

H 2<br />

‣ Con<strong>for</strong>mable shape liquid<br />

tank with design to<br />

separate liquids; 22.5<br />

gallons <strong>for</strong> 5 kg hydrogen<br />

at 6 wt. % and unit density<br />

‣ Heat exchange reduces<br />

the vehicles’ radiator load<br />

by ca. 40% (<strong>for</strong> ∆H of 12<br />

kcal/mol H 2 and 50% FC<br />

efficiency)<br />

LQ*H 2<br />

+ heat (∆H)<br />

Catalyst<br />

P < 10 atm.<br />

P > 50 atm.<br />

Catalyst<br />

LQ + H 2<br />

Maximum energy efficiency: by (a) recovering the<br />

exothermic (-∆H) of hydrogenation and (b) utilizing the<br />

waste heat from the power source to supply the ∆H <strong>for</strong><br />

the endothermic dehydrogenation.<br />

6<br />

© Air Products and Chemicals, Inc, 2006

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