BACKGROUND: Diffusion distillation of ethanol-water mixtures in the presence of air as an inert gas has been used to produce fuel grade ethanol, and studies on the effect of vaporization temperature and feed composition on the selectivity and total molar flux have been presented recently. This paper
The effect of water vapor and inert gases on the carbon-oxygen reaction
β Scribed by S. Ahmed; M.H. Back
- Publisher
- Elsevier Science
- Year
- 1987
- Tongue
- English
- Weight
- 695 KB
- Volume
- 25
- Category
- Article
- ISSN
- 0008-6223
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β¦ Synopsis
The interpretation of the effect of small quantities of water vapor on the kinetics of the gasification of carbon by oxygen is re-examined in the light of recent studies describing conditions under which an explosive reaction may occur in this mixture of reactant and products: oxygen, carbon monoxide, carbon dioxide and water vapor. The generation of water from residual hydrogen in the carbon is a key factor in the development of explosive conditions through a radical chain reaction in the gas phase. Some effects of inert gases on the rate of gasification are also explained by their influence on gas-phase reactions through stabilization of radicals and inhibition of diffusion of atoms to the walls. It is concluded that the possibility of gas-phase radical reactions in mixtures of carbon monoxide and oxygen, which depends critically on the presence of water vapor, should be considered in the interpretation of the kinetics of carbon gasification by oxygen. Key Words-Gasification, oxygen, effect of water vapor, gas phase reactions, inert gases, carbonoxygen reaction.
THE EFFZCT OF WATER VAPOR ON THE
CARBON-OXYGEN REACTION
π SIMILAR VOLUMES
The effect of diluent gases on gasification rates of the C-O, and C-CO2 reactions has been studied. At equal starting pressures of reactant and diiuent, rates for both reactions are: Nz > Ar > He. For the C-CO, reaction, the presence of a diiqent results in higher gasification rates than when no dil
The reaction of Graphon with O2 has been studied at 625Β°C in a static system, using initial O2 pressures between 25 and 750 mTorr. and samples pre-oxidized to varying degrees of burn-off between 0 and 20 per cent. The reaction temperature was low enough for secondary reactions to be neglected. A mas