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II International Symposium on Carbon for Catalysis ABSTRACTS

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IS IT POSSIBLE TO SOLVE THE HYDROGEN STORAGE PROBLEM<br />

WITH ACTIVATED CARBONS<br />

KL-1<br />

Fenel<strong>on</strong>ov V.B., Ustinov E.A., Yakovlev V. 1 , Barnakov Ch.N.<br />

Boreskov Institute of <strong>Catalysis</strong> SB RAS, Novosibirsk, Russia<br />

1 Scientific and Producti<strong>on</strong> Company “Provita”, St Petersburg, Russia<br />

e-mail: fenel<strong>on</strong>@catalysis.ru<br />

One of the key problems in the development of hydrogen-fueled vehicles is c<strong>on</strong>nected with<br />

the hydrogen storage. The complexity of the hydrogen storage is due to its “simple”<br />

molecular structure. The hydrogen molecule has <strong>on</strong>ly two electr<strong>on</strong>s, which is the reas<strong>on</strong> of an<br />

extremely weak intermolecular interacti<strong>on</strong>. As a c<strong>on</strong>sequence, it has low melting point (14.01<br />

K), low boiling point (20.3 K), low critical temperature (33.2 K), and low densities of all<br />

phases etc. Those complicati<strong>on</strong>s have led to a search <strong>for</strong> soluti<strong>on</strong>s of the storage of hydrogen<br />

as a n<strong>on</strong>-traditi<strong>on</strong>al fuel. At the present time there are several ways of soluti<strong>on</strong> of the problem,<br />

which are based <strong>on</strong> the following approaches: А) deriving hydrogen directly at the vehicle by<br />

a catalytic re<strong>for</strong>ming of hydrocarb<strong>on</strong>s; B) hydrogen storage in regenerated chemical<br />

adsorbents <strong>on</strong> the basis of metal hydrides of bor<strong>on</strong>, lithium, aluminates, etc.; C) physical<br />

adsorpti<strong>on</strong> in fine-porous adsorbents; D) the use of compressed GH 2 at 35-70 MPa, and E)<br />

cryogenic LH 2 .<br />

Each of the above methods has its principal drawback. The method A) does not solve the<br />

problem of the carb<strong>on</strong> dioxide emissi<strong>on</strong>. Applicati<strong>on</strong> of the method B) with solid regenerated<br />

chemical adsorbents is complicated by their phase and volume changes during adsorpti<strong>on</strong> and<br />

desorpti<strong>on</strong> of hydrogen. The method D) is dangerous because of a possibility of instantaneous<br />

release of mechanical energy of the compressed gas during an emergency. The method E),<br />

much as it is seemed a bit exotic (the storage of H 2 at ~20 K, slush hydrogen at ~14 K, or<br />

compressed hydrogen at 30-50 K) has been tested in rocket and space technology l<strong>on</strong>g ago.<br />

Modern Dewar c<strong>on</strong>tainers with multi-layer vacuum thermal insulati<strong>on</strong> virtually allow keeping<br />

LH 2 <strong>for</strong> several weeks without any losses. The principal drawback of this method is<br />

associated not with the problem of storage in itself, but with power inputs required to<br />

refrigerate Н 2 up to the temperature of liquefacti<strong>on</strong>.<br />

Minimal power inputs L required <strong>for</strong> obtaining the unit of cooling Q in the process of<br />

cooling of hydrogen from the initial temperature Т 0 down to the final temperature T is<br />

19

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