Process and apparatus for production of elemental sulfur
AssigneeDavy International Aktiengesellschaft
InventorGhazi R. Al-Muddarris
Life of this patent
Estimating the term…
Abstract
A process is provided involving the production of elemental sulfur via the Claus reaction of hydrogen sulfide and sulfur dioxide. A gas feedstream containing H.sub.2 S and SO.sub.2 is passed through solid catalyst beds below the sulfur dew point to thereby deposit the sulfur formed on the catalyst bed. Sulfur is then removed from the catalyst bed by passing heated effluent gas from another catalyst bed through the first bed to vaporize the deposited sulfur and thereby regenerate the first catalyst bed. Reactor apparatus especially suitable for practicing this process is also provided.
Claims16
In the process for reacting a gas containing hydrogen sulfide and sulfur dioxide to form elemental sulfur via the Claus reaction, wherein said gas is passed through a plurality of solid catalyst beds at an elevated temperature which is below the sulfur dew point, to thereby charge said catalyst beds with at least a part of the sulfur formed and wherein said catalyst beds are subsequently regenerated by passing heated gas therethrough, the improvement which comprises:
- (A) passing the hydrogen sulfide and sulfur dioxide containing gas during a charging phase through a first catalyst bed at a temperature below the sulfur dew point so as to charge the bed with sulfur;
- (B) heating all effluent from the first catalyst bed during a first part of the first catalyst bed charging phase to a temperature above the sulfur dew point;
- (C) passing said heated effluent to a sulfur-containing second catalyst bed in order to vaporize sulfur from said second catalyst bed and to thereby regenerate said second catalyst bed;
- (D) discontinuing the heating of said first catalyst bed effluent during a second part of the first catalyst bed charging phase such that the temperature of said effluent falls below the sulfur dew point;
- (E) passing said cooler effluent through said regenerated second catalyst bed to thereby cool said regenerated second catalyst bed;
- (F) passing the effluent from the second catalyst bed through a sulfur condenser so as to condense vaporized sulfur contained in the effluent;
- (G) withdrawing sulfur condenser waste gas directly from the process;
- and
- (H) reversing the direction of flow of the gas through said first and second catalyst beds after the first catalyst bed has been charged with sulfur.
Dependencies are inferred from the claim text.