Hydrogen sulfide removal process

1. A process to treat hydrogen sulfide present in a gas stream comprising:

directing the gas stream containing hydrogen sulfide into an absorber and separator combination comprising two vertical parallel columns, where the first column is in fluid communication with the second column such that a bottom of the first column is connected to a bottom portion of the second column and where the gas stream is introduced into a top portion of the first column in a first direction such that it moves down the first column;

injecting a first stream of liquid treatment solution comprising a chelated metal catalyst into the gas stream through a jet nozzle positioned within the first column at a position where the first jet nozzle is oriented to cause the liquid treatment solution to flow in a second direction upward and into the gas stream to create a first turbulent mixing zone adjacent to the first jet nozzle;

maintaining the flow rate of the gas stream within the first column such that the flow of the liquid treatment solution is reversed to flow in the first direction;

absorbing the hydrogen sulfide into the liquid treatment solution within the turbulent zone to create an admixture of treated gas and spent liquid treatment solution;

discharging the admixture from the bottom of the first column directly into the bottom of the second column, where the admixture enters into a settling section;

separating the treated gas from the admixture and discharging the treated gas from a top portion of the second column; and

removing the spent liquid treatment solution from the settling section.

2. The process of claim 1 , wherein the liquid treatment solution is injected into the first column through two or more jet nozzles.

3. The process of claim 1 further comprising, introducing the removed spent liquid treatment solution into an oxidizer;

contacting the spent liquid treatment solution with an oxygen containing gas within the oxidizer to form a regenerated treatment solution comprising elemental sulfur; and

removing excess oxygen containing gas from the oxidation vessel and separately removing the regenerated liquid treatment solution from the oxidizer.

4. The process of claim 3 further comprising,

recycling a portion of the removed regenerated liquid treatment solution for introduction into the jet nozzle.

5. A process to treat hydrogen sulfide present in a gas stream comprising:

directing the gas stream containing hydrogen sulfide a hydrocarbon into an absorber and separator combination comprising two vertical parallel columns, where the first column is in fluid communication with the second column such that a bottom of the first column is connected to a bottom portion of the second column, where the gas stream is introduced into a top section of an absorber column to cause the gas stream to flow downward within the absorber column;

injecting a first stream of liquid treatment solution comprising a chelated metal catalyst into the gas stream through a first jet nozzle positioned within the first column at a position below the top section of the first column, where the first jet nozzle is oriented to cause the liquid treatment solution to be initially directed upward into the downward flowing gas stream to create a first turbulent mixing zone above the first jet nozzle;

maintaining the flow rate of the gas stream within the first column such that the initial upward flow of the liquid treatment solution is reversed to a downward directed flow;

absorbing the hydrogen sulfide into the liquid treatment solution within the turbulent zone to create an admixture of treated gas and spent liquid treatment solution;

discharging the admixture from the bottom of the first column and directly into a bottom section of the second column;

separating the treated gas comprising the hydrocarbon from the admixture and discharging the treated gas from a top section of the second column; and

removing the spent liquid treatment solution from the bottom section of the second column.

6. The process of claim 5 further comprising, introducing the removed spent liquid treatment solution to a top section of an oxidizer;

contacting the spent liquid treatment solution with an oxygen containing gas within the oxidizer to form a regenerated treatment solution comprising elemental sulfur; and

removing excess oxygen containing gas from the oxidation vessel and separately removing the regenerated liquid treatment solution from the oxidizer.

7. The process of claim 6 further comprising,

recycling the removed regenerated liquid treatment solution for introduction into the jet nozzle.

8. The process of claim 5 further comprising,

injecting a second liquid treatment solution comprising a chelated metal catalyst into the first column through a second jet nozzle positioned within the first column at a position below the first jet nozzle, where the jet nozzle is oriented to cause the liquid treatment solution to be initially directed upward to create a second turbulent mixing zone above the second jet nozzle and below the first jet nozzle.

9. The process of claim 7 where a make-up catalyst stream is mixed with the regenerated liquid treatment solution to form part of the liquid treatment solution injected into the first jet nozzle.

10. The process of claim 6 where a portion of the regenerated liquid treatment solution is introduced into sulfur recovery process where elemental sulfur is recovered as a byproduct and a substantially sulfur free liquid treatment solution is recovered for recirculation as part of the liquid treatment solution injected into the first jet nozzle.

11. The process of claim 5 where the treated gas is passed through a mist eliminator before discharging the treated gas from the top section of the second column.

12. The process of claim 5 where flow rates of the stream of process gas and of the liquid treatment solution within the first column are controlled to be below flooding velocity.

13. The process of claim 5 where flow rates of the stream of process gas and of the liquid treatment solution within the first column are controlled to be about 25% of flooding velocity.