Zero emissions sulphur recovery process with concurrent hydrogen production
Disclosed is a process for the concurrent production of hydrogen and sulphur from a H 2 S-containing gas stream, with reduced, and preferably zero, emissions. The method comprises the catalytic oxidative cracking of H 2 S so as to form H 2 and S 2 . Preferably, the oxidation is conducted using oxygen-enriched air, preferably pure oxygen. The process is conducted in a reaction chamber comprising a bifunctional catalyst material, so as to favor both the partial oxidation of H 2 S and the dissociation thereof.
1. A plant suitable for conducting catalytic oxidative cracking of an H 2 S-containing gas stream, said plant comprising a catalytic reaction chamber having a first inlet for an H 2 S-containing acid gas stream and a second inlet for an oxygen-comprising stream and comprising a reaction zone containing in series a first catalyst bed filled with a first catalyst for H 2 S partial oxidation and downstream thereof a second catalyst bed filled with a second catalyst for H 2 S cracking;
wherein the first catalyst is an oxidation catalyst selected from the group consisting of one or more Group VIII metals and oxides thereof and the second catalyst is a cracking catalyst which is one or more metal sulphides; and
wherein the reaction chamber further comprises a gas quench zone downstream from the reaction zone; and
wherein said plant further comprises, upstream of said catalytic beds, a static mixer configured for mixing gases from said first and second inlets.
2. A plant according to claim 1 , wherein said gas quench zone comprises a water sprayer.
3. The plant according to claim 1 , wherein the second catalyst is selected from the group consisting of CoS 2 , NiS, NiS 2 , WS 2 , MoS 2 , FeS 2 , Ag 2 S, CuS, CdS, MnS, ZnS, and Cr 2 S 3 .
4. The plant according to claim 1 which further comprises a waste heat boiler and a sulphur condenser downstream of the reaction chamber.