Thermochemical cycles where metal oxides are reduced and the elementary met
al is reoxidized with water, thus generating hydrogen has been proposed for
conversion of solar energy to chemical energy and fuels. The two steps of
the cycle can be separated in time and place, thus providing also means for
storage of solar energy in chemical form. The second step of these cycles
involves the oxidation of the elementary metal in water vapor where hydroge
n is generated and the metal oxide is recovered and recycled. Reduction of
zinc oxide is a typical reaction used for such cycles. Therefore, the oxida
tion of liquid zinc with water, specifically, becomes an important part of
such a cycle. The kinetics of oxidation of bulk of liquid zinc at 450-500 d
egrees C, with water vapors bubbled through the liquid, was studied. The wa
ter vapor was introduced into the liquid using argon as a carrier gas. The
water vapor partial pressure was in the range of 65-560 mb. The gas mixture
was fed through a tube dipped in the liquid. The diameter of the tube and
its depth were varied as parameters of the experiments. The results of the
experiments show that the specific reaction rate (hydrogen production per c
m(2) of surface area of the bubble), W-sp, increases, as the water partial
pressure is increased. The order of the reaction, with respect to water par
tial pressure, is 0 < n < 1. As a result of the experiments, the kinetic ex
pression W-sp = kP(H2)O/(1+ b.PH2O) was found: k = 1.86 x 10(-3).EXP(-40376
/RT) mole.cm(-2).s(-1)bar(-1), b = 1.55 x 10(-10).EXP(146330/RT) bar(-1). T
he main stages of the reaction are interaction between elementary zinc and
water vapor on the interface between the gas and the solid oxide layer, and
the diffusion of zinc atoms through the film of solid zinc oxide. (C) 2000
International Association for Hydrogen Energy. Published by Elsevier Scien
ce Ltd. All rights reserved.