Method for removal of hydrogen sulfide from geothermal steam and condensate
View Patent ↗A method for scavenging hydrogen sulfide from geothermal steam in a condenser under vacuum. A fine curtain of atomized acrolein-water droplets may be sprayed into geothermal steam condensers in an amount of approximately 2:1 molar ratio of acrolein to H 2 S based on hydrogen sulfide in the incoming steam from the turbine. The range being approximately 0.1 ppm to 500 ppm of sulfide. The acrolein is allowed to react with the gas phase H 2 S to form non-volatile aldehyde byproducts which partition into the water phase, are returned to the cooling tower and ultimately removed by normal cooling-tower blow down.
1. A system comprising:
a cooling tower comprising cooling water;
an acrolein feed line in fluid communication with the cooling tower;
a condenser, where the condenser is in fluid communication with the cooling tower through a flow line;
a geothermal steam line in fluid communication with the condenser; and
a plurality of spray nozzles, the spray nozzles in fluid communication with the flow line and adapted to spray acrolein-water droplets inside the condenser.
2. The system of claim 1 , further comprising:
an acrolein reservoir in fluid communication with the acrolein feed line; and
a bisulfate scrubber in fluid communication with the acrolein reservoir.
3. The system of claim 1 further comprising:
a cooling water return line in fluid communication with the cooling tower and the condenser.
4. The system of claim 1 , further comprising:
a cooling tower sump outlet line in fluid communication with the cooling tower and the flow line; and
an acrolein injector in fluid communication with the acrolein feed line and the cooling tower sump outlet line.
5. The system of claim 1 further comprising a hydrogen sulfide sensor adapted to measure hydrogen sulfide in a non-condensible gas layer in the condenser.
6. The system of claim 1 , wherein the acrolein-water droplets comprise acrolein the aqueous phase.
7. The system of claim 1 wherein the condenser is under vacuum.
8. The system of claim 1 , wherein the geothermal steam line comprises geothermal steam from power plant turbines and wherein the geothermal steam comprises hydrogen sulfide.
9. The system of claim 8 , wherein the condenser is adapted to react the hydrogen sulfide from in the geothermal steam in the vapor phase with the acrolein-water droplets.
10. The system of claim 9 , wherein the condenser has a temperature of approximately 250° F.
11. The system of claim 9 , wherein the amount of acrolein in the acrolein water droplets is approximately 0.1 ppm to approximately 20 ppm per hydrogen sulfide (w/w) in the geothermal steam.