Efficient Generation of H 2 by Splitting Water with an Isothermal Redox Cycle
Isothermal Water Splitting Solar concentrators can create extremely high temperatures that can drive chemical reactions, including the thermal splitting of water to provide hydrogen. A metal oxide catalyst is needed that is usually cycled between hotter conditions where it is reduced and cooler cond...
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Published in | Science (American Association for the Advancement of Science) Vol. 341; no. 6145; pp. 540 - 542 |
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Main Authors | , , , , , , , |
Format | Journal Article |
Language | English |
Published |
02.08.2013
|
Online Access | Get full text |
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Summary: | Isothermal Water Splitting
Solar concentrators can create extremely high temperatures that can drive chemical reactions, including the thermal splitting of water to provide hydrogen. A metal oxide catalyst is needed that is usually cycled between hotter conditions where it is reduced and cooler conditions where it is reoxidized by water. This cycling can limit catalyst lifetime, which can be costly.
Muhich
et al.
(p.
540
; see the Perspective by
Roeb and Sattler
) developed an approach that allowed the redox cycle to be driven isothermally, using pressure swings.
A thermal process for generating H
2
from water uses pressure changes to recycle between catalyst redox states.
[Also see Perspective by
Roeb and Sattler
]
Solar thermal water-splitting (STWS) cycles have long been recognized as a desirable means of generating hydrogen gas (H
2
) from water and sunlight. Two-step, metal oxide–based STWS cycles generate H
2
by sequential high-temperature reduction and water reoxidation of a metal oxide. The temperature swings between reduction and oxidation steps long thought necessary for STWS have stifled STWS’s overall efficiency because of thermal and time losses that occur during the frequent heating and cooling of the metal oxide. We show that these temperature swings are unnecessary and that isothermal water splitting (ITWS) at 1350°C using the “hercynite cycle” exhibits H
2
production capacity >3 and >12 times that of hercynite and ceria, respectively, per mass of active material when reduced at 1350°C and reoxidized at 1000°C. |
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ISSN: | 0036-8075 1095-9203 |
DOI: | 10.1126/science.1239454 |