Review of Small Stationary Reformers for Hydrogen Production
Review of Small Stationary Reformers for Hydrogen Production
Review of Small Stationary Reformers for Hydrogen Production
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Delivered Cost <strong>of</strong> H2 ($/GJ)<br />
30<br />
25<br />
20<br />
15<br />
10<br />
Figure 3.<br />
5<br />
0<br />
Delivered Cost <strong>of</strong> <strong>Hydrogen</strong><br />
Transportation Fuel ($/GJ)<br />
LH2 Truck Delivery<br />
Central SMR - pipeline deliv. - lo density<br />
Central SMR - pipeline deliv. -hi density<br />
Onsite adv. SMR<br />
Onsite adv. electrolysis<br />
39<br />
REFORMER<br />
NATURAL GAS<br />
CENTRAL H2 PRODUCTION<br />
PIPELINE H2 T&D<br />
ELECTROLYZER CAPITAL+O&M<br />
STORAGE CYLINDERS<br />
COMPRESSOR CAPITAL+O&M<br />
ELECTRICITY<br />
LIQUID HYDROGEN<br />
LH2 TANK+PUMP<br />
DISPENSER<br />
LABOR<br />
NG costs $3/MBTU;<br />
<strong>of</strong>f-peak power costs 3<br />
cents/kWh.<br />
Each refueling station<br />
dispenses 1 million scf<br />
H2/day.
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