Process of removing of COS and CS.sub.2 compounds contained in an industrial gas
AssigneeSociete Nationale Elf Aquitaine (Production)
InventorRobert Voirin
Life of this patent
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Abstract
A process is provided for eliminating COS and CS.sub.2 compounds contained in an industrial gas. The gas containing an appropriate quantity of water vapor is contacted with a titanium oxide catalyst arranged in a high temperature reaction zone. The reaction is carried out while maintaining at specific values the ratio R between the number of water vapor moles and the number of moles of the compound(s) COS and CS.sub.2 in the supplied gas in contact with the catalyst, as well as the temperature at the outlet from the reaction zone. The process is applicable to the treatment of industrial gases usable in organic synthesis and containing COS and CS.sub.2 as impurities susceptible of perturbating synthesis reactions.
Claims12
A process for the reduction of COS and CS.sub.2 compounds contained in concentrations of from 0.01 to 6% by volume in a gas containing water vapor which comprises:
- contacting the gas containing water vapor, in a reaction zone, with a catalyst selected from the group consisting of (a) titanum dioxide, (b) a mixture of titanium dioxide with a sulfate of an alkaline earth metal selected from the group consisting of Ca, Ba, Sr and Mg in a weight ratio of titanium dioxide, expressed as TiO.sub.2, to alkaline earth metal sulfate of from about 99:1 to about 6:4 or (c) a mixture of (a) or (b) with up to about 30% by weight, of the mixture, of at least one composition selected from the group consisting of silica, clay, alumina, silicates, titanium sulfate and ceramic fibers;
- controlling the quantity of water vapor present in the gas in contact with the catalyst in a manner such that in said gas the R ratio of the number of moles of water vapor to the number of moles of COS and CS.sub.2 compounds present in the gas have a value of from the stoichiometric value corresponding to a complete hydrolysis of said compounds to 50/1+1.5 p, with p representing the molar fraction of CS.sub.2 in the total molar quantity of COS and CS.sub.2 contained in the gas;
- and by maintaining the temperature in the reaction zone at a value corresponding to the temperature at the exit of said zone comprised between .phi..sub.1 =100 (0.6+1.6q).degree.C. and .phi..sub.2 =100 (2.2+q).degree.C., wherein q has a value of zero when p has a value of from 0 to 0.1, or the value 1 when p has another value.
Dependencies are inferred from the claim text.