Method and system for catalytic oxidation of a lean H
The present invention relates to a method and a system for catalytic oxidation of a lean H 2 S stream. More specifically, the invention concerns a novel way of removing sulfur dioxide (SO 2 ) formed by catalytic oxidation of hydrogen sulfide (H 2 S) with the purpose of removing H 2 S from a gas. This catalytic oxidation of H 2 S yields sulfur dioxide (SO 2 ) through the use of known catalysts, so-called SMC catalysts.
1. A method for the oxidation of hydrogen sulfide, carbonyl sulfide or carbon disulfide to sulfur dioxide, said method comprising the steps of:
providing a feed gas lean in H 2 S,
adding air or O 2 to the feed gas,
heating the feed gas to the desired inlet temperature,
feeding the gas mixture to an oxidation reactor, which contains an oxidation catalyst, and
recovering a cleaned gas,
wherein syngas is added to the gas mixture prior to feeding the gas mixture to the oxidation reactor, and
wherein the feed gas is heated in the absence of a burner.
2. The method according to claim 1 , wherein the oxidation catalyst is a sulfur monolith catalyst.
3. The method according to claim 1 , wherein the gas mixture is fed to the oxidation reactor via a heat exchanger.
4. The method according to claim 1 , wherein the oxidation of H 2 S proceeds at an inlet temperature to the catalyst between 200 and 450° C.
5. The method according to claim 4 , wherein the inlet temperature to the catalyst is between 200 and 400° C.
6. The method according to claim 4 , wherein the inlet temperature to the catalyst is between 250 and 400° C.
7. The method according to claim 1 , wherein the inlet temperature to the catalyst is between 250 and 300° C.
8. The method according to claim 1 , wherein said oxidation is carried out through catalytic oxidation.
9. The method according to claim 1 , wherein said oxidation is not carried out through combustion.
10. A system for carrying out the method according to claim 1 for the oxidation of hydrogen sulfide to sulfur dioxide, said system comprising a gas blower, a heat exchanger and an oxidation reactor, which contains a catalyst, and wherein said system does not comprise a burner.
11. The system according to claim 10 , wherein the catalyst is a sulfur monolith catalyst.
12. The system according to claim 10 , comprising only one gas blower.