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Recent Developments in the Homogeneous Catalysis of the Water-Gas Shift Reaction

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Aspects of Homogeneous Catalysis

Part of the book series: Aspects of Homogeneous Catalysis ((AHCA,volume 5))

Abstract

The major portion of the world’s hydrogen supply is derived from steam cracking of hydrocarbons, particularly methane and naphtha, which produces water-gas:

$$ {C_x} + {H_2}O\xrightarrow{{catalyst}}CO + {H_2} + C{O_2} $$
(1)

Stripping the water-gas mixture of CO2 and any residual water gives syngas (CO/H2). If a particular industrial process using syngas requires that the ratio of CO to H2 in the syngas coming from (1) be adjusted in favor of H2 or if only pure H2 is required, as it would be in ammonia synthesis, then it is possible to catalytically convert the reducing equivalents of CO to H2 via the water-gas shift reaction (WGSR):

$$ {H_2}O + CO\xrightarrow{{catalyst}}{H_2} + C{O_2} $$
(2)
$$ \Delta G = - 6.82kcal/mol,\Delta H = - 9.84,\Delta S = - 10.1eufor{H_2}O\left( g \right)at{298^o}C $$
$$ \Delta G = - 4.76kcal/mol,\Delta H = 0.68,\Delta S = + 18.3eufor{H_2}O\left( \ell \right)at{298^o}G $$

In effect, the WGSR is another major source of the world’s hydrogen.

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Laine, R.M., Wilson, R.B. (1984). Recent Developments in the Homogeneous Catalysis of the Water-Gas Shift Reaction. In: Ugo, R. (eds) Aspects of Homogeneous Catalysis. Aspects of Homogeneous Catalysis, vol 5. Springer, Dordrecht. https://doi.org/10.1007/978-94-009-6363-4_4

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  • DOI: https://doi.org/10.1007/978-94-009-6363-4_4

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