NIPPON KAGAKU KAISHI
Online ISSN : 2185-0925
Print ISSN : 0369-4577
The Hydrolysis of Iron(II) Bromide
Hiroshi ISHIKAWAEiichi ISHIIItsuki UEHARAMasanori NAKANEYoshizo MIYAKE
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1978 Volume 1978 Issue 4 Pages 530-534

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Abstract

As a fundamental study on thermochemical production of hydrogen from water, the hydro-lysis of iron (II) bromide
3 FeBr2+4 H2O →Fe3O4 + 6 HBr+ H2 (1)
FeBr2 + H2O → FeO + 2 HBr (2)
has been investigated. First, solid FeBr2 was hydrolyzed at ca. 490°C according to the equation (1), and the maximum amount of hydrogen in the highest yield was obtained at 620°C. The hydrolysis reaction was carried out by using a fixed bed reactor (25 mmΦ) charged with 120 g of FeBr2 at 620°C. The maximum conversion rate of water was 10% at 30 g/hr of feed rate of H2O, and the rate increased gradually with decreasing feed rate of H2O, i. e., 11% at 20 g/hr and 13% at 10 g/hr. These higher values than that predicted by thermodynamic calculation, i. e., 9. 2%, suggested that sublimed FeBr2 was also hydrolyzed.
Second, the hydrolysis of molten FeBr2 was carried out by bubbling vaporized water through the molten salt at 700°C. At the initial stage of the reaction, FeBr2 was hydrolyzed according to the equation (2) resulting FeO, and the conversion rates of water were higher than those in solid-gas reaction mentioned above. But continuous run of the reaction was difficult because resulting iron oxide closed the water feed pipe.
Third, the hydrolysis of vaporized FeBr2 was also carried out in a flow system at 800∼900°C. In this case, FeBr2 was hydrolyzed in terms of the both equation, (1) and (2). The fractions of FeBr2 hydrolyzed according to these competitive reactions depended on a H2O to FeBr2 ratio.

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