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Biofuels in Perspective

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Biological Hydrogen Production by Anaerobic Microorganisms 213<br />

hydrogen formation from ferredox<strong>in</strong> is thermodynamically more favorable (vide <strong>in</strong>fra),<br />

Pyrococcus should be able to produce hydrogen more easily. However, batch cultur<strong>in</strong>g has<br />

shown that <strong>in</strong> addition to acetate, CO2 and alan<strong>in</strong>e, P. furiosus produces ∼2.6–3.0 H2 per<br />

glucose equivalent, 29 which is not superior to the mesophiles, and even worse compared<br />

to Tt. maritima. Nevertheless, the amount of hydrogen that is produced is strongly <strong>in</strong>fluenced<br />

by the P(H2). 29 At low P(H2) more hydrogen (3.7 H2/glucose) is produced as was<br />

shown by cocultur<strong>in</strong>g of P. furiosus with a hyperthermophilic methanogen. Likewise, <strong>in</strong><br />

substrate-limited chemostat cultures, dur<strong>in</strong>g N2-flush<strong>in</strong>g, hydrogen levels amounted to 3.9<br />

H2 per glucose (Tu<strong>in</strong><strong>in</strong>ga and Kengen unpublished results).<br />

The enzyme <strong>in</strong>volved <strong>in</strong> transfer of the electrons (ferredox<strong>in</strong>) to hydrogen has been <strong>in</strong>vestigated<br />

<strong>in</strong> detail for P. furiosus. 30,83 P. furiosus conta<strong>in</strong>s two cytoplasmic [NiFe]-conta<strong>in</strong><strong>in</strong>g<br />

hydrogenases (Sulfhydrogenase I and II) that are capable of reduc<strong>in</strong>g protons to hydrogen<br />

but also to reduce polysulfide to H2S (37, 91) (Table 11.3). However, NADPH is the preferred<br />

electron donor for these bifunctional enzymes and not ferredox<strong>in</strong>. A third cytopasmic<br />

enzyme has been described, which conta<strong>in</strong>s Fe-S centers and a flav<strong>in</strong> and which is also<br />

capable of polysulfide reduction. In addition, this sulfide dehydrogenase was shown to have<br />

ferredox<strong>in</strong>:NADP oxidoreductase activity, and it was therefore <strong>in</strong>itially hypothesized that<br />

reductant is transferred via ferredox<strong>in</strong> to NADP and subsequently to hydrogen. 47 However,<br />

Silva et al. showed that the turnover of the sulfhydrogenase is too low to account for the flux<br />

of reductant from the glycolysis. Moreover, they could demonstrate that P. furiosus conta<strong>in</strong>s<br />

another membrane-bound [Ni-Fe] hydrogenase complex which can accept electrons from<br />

ferredox<strong>in</strong> directly, without the <strong>in</strong>volvement of NADP(H). This hydrogenase complex is<br />

encoded by the mbh operon, consist<strong>in</strong>g of 14 ORFs. This hydrogenase was found to be<br />

unique <strong>in</strong> that it is rather resistant to <strong>in</strong>hibition by CO and that it exhibits an extremely<br />

high H2 evolution to H2 uptake activity ratio compared to other hydrogenases. 83 Moreover,<br />

it was shown that the enzyme could act as a proton pump, generat<strong>in</strong>g a proton-motive<br />

force, and coupled to the synthesis of ATP. 30 The genome conta<strong>in</strong>s a second gene cluster<br />

(mbx operon) cod<strong>in</strong>g for another [NiFe]-conta<strong>in</strong><strong>in</strong>g hydrogenase complex, and highly<br />

homologous to the mbh cluster (Table 11.3). Its physiological role is as yet unknown.<br />

The ferredox<strong>in</strong>:NADP oxidoreductase (or sulfide dehydrogenase) can become active<br />

under conditions of high P(H2), by transferr<strong>in</strong>g electrons from ferredox<strong>in</strong> to<br />

polysulfide or to NADP. Subsequently, NADPH can be reoxidized by produc<strong>in</strong>g alan<strong>in</strong>e<br />

from pyruvate us<strong>in</strong>g glutamate dehydrogenase (NADP-dependent) and alan<strong>in</strong>e<br />

am<strong>in</strong>otransferase. 92<br />

11.11 Approaches for Improv<strong>in</strong>g Hydrogen Production<br />

Ways to improve fermentative hydrogen production have been reviewed by Nath and<br />

Das. 93 Improvements can be made by the proper choice of the fermentative bacterium, by<br />

apply<strong>in</strong>g genetic modification to redirect biochemical pathways <strong>in</strong> such a way that less side<br />

products are formed and by a proper process design and process operation (gas sparg<strong>in</strong>g,<br />

creat<strong>in</strong>g a large biofilm surface, etc.). All these measures will optimize hydrogen formation<br />

only to maximally 4 molecules of hydrogen per molecule of glucose and may result <strong>in</strong> an<br />

<strong>in</strong>crease of the hydrogen production rate. However, the challenge is to extend the yield to<br />

more than 4 hydrogen per glucose. In pr<strong>in</strong>ciple this might be possible by block<strong>in</strong>g certa<strong>in</strong>

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