Chemical solution and methods of using same for remediating hydrogen sulfide and other contaminants in petroleum based and other liquids
A treatment process for remediating a contaminated liquid containing more than 5 ppm hydrogen sulfide, includes steps of: preparing a treatment solution containing an aqueous solution containing ≥1 hydroxide compound, in which a collective concentration of the ≥1 hydroxide compound in the aqueous solution is in a range of 35-55 weight percent and the aqueous solution constitutes at least 95% of the treatment solution; adding to the liquid an amount of an treatment solution sufficient to reduce a concentration of hydrogen sulfide in the contaminated liquid to ≤5 ppm based on stoichiometry of reactions between the ≥1 hydroxide compound and the hydrogen sulfide in the liquid; and dispersing the treatment solution in the liquid and allowing the treatment solution to react with the contaminated liquid for a period of time until a concentration of hydrogen sulfide in the liquid is reduced to ≤5 ppm.
1. A stand-alone aqueous treatment solution for directly remediating hydrogen sulfide (H 2 S) and other contaminants in liquids, the treatment solution consisting of:
at least one hydroxide compound; and
an antibacterial agent, wherein
a collective concentration of the at least one hydroxide compound in the aqueous treatment solution is in a range of 35-55 weight percent,
the antibacterial agent is at least one of a silicate compound and barium, and
collectively the at least one hydroxide compound and water constitute at least 95 weight percent of the aqueous treatment solution.
2. The aqueous treatment solution according to claim 1 , wherein the collective concentration of the at least one hydroxide in the aqueous solution is 45-55 weight percent.
3. The aqueous treatment solution according to claim 1 , wherein the aqueous treatment solution contains at least two different hydroxide compounds.
4. The aqueous treatment solution according to claim 1 , wherein the aqueous treatment solution contains sodium hydroxide (NaOH) and potassium hydroxide (KOH).
5. The aqueous treatment solution according to claim 1 , wherein a silicate compound is the antibacterial agent and the silicate compound is added at a concentration of 0.1-2 weight percent in the aqueous treatment solution.
6. A treatment process for preparing a remediated liquid from a contaminated liquid originally containing more than 5 ppm hydrogen sulfide (H 2 S), comprising steps of:
preparing a stand-alone aqueous treatment solution consisting of water, at least one hydroxide compound and an antibacterial agent, in which a collective concentration of the at least one hydroxide compound in the aqueous treatment solution is in a range of 35-55 weight percent and collectively the at least one hydroxide compound and the water constitute at least 95 weight percent of the aqueous treatment solution;
adding to the contaminated liquid an amount of the aqueous treatment solution sufficient to reduce a concentration of hydrogen sulfide in the contaminated liquid to ≤5 ppm based on stoichiometry of reactions between the at least one hydroxide compound and the hydrogen sulfide in the contaminated liquid; and
dispersing the aqueous treatment solution in the contaminated liquid and allowing the aqueous treatment solution to react with the contaminated liquid for a period of time until a concentration of hydrogen sulfide in the contaminated liquid is reduced to ≤5 ppm due to the reactions between the at least one hydroxide compound and the hydrogen sulfide in the contaminated liquid.
7. The treatment process according to claim 6 , wherein the amount of the aqueous treatment solution added to the contaminated liquid is within a range of 0.25-6.0 ml/liter of the contaminated liquid.
8. The treatment process according to claim 7 , wherein
the contaminated liquid is a petroleum based liquid, and
the amount of the aqueous treatment solution added to the contaminated liquid is adjusted within the range of 0.25-6.0 ml/liter of the contaminated liquid based on at least one of the concentration of hydrogen sulfide in the contaminated liquid; a desired reaction time for reducing the concentration of hydrogen sulfide in the contaminated liquid to ≤5 ppm; and a viscosity of the contaminated liquid.
9. The treatment process according to claim 7 , wherein
the contaminated liquid is a an aqueous solution, and
the amount of the aqueous treatment solution added to the contaminated liquid is adjusted within the range of 0.25-6.0 ml/liter of the contaminated liquid based on at least one of the concentration of hydrogen sulfide in the contaminated liquid and a desired reaction time for reducing the concentration of hydrogen sulfide in the contaminated liquid to ≤5 ppm.
10. The treatment process according to claim 7 , wherein the treatment process comprises an further step of adding to the contaminated liquid an additional amount of the aqueous treatment solution to cause a precipitate containing sulfur to be generated from the treated, contaminated liquid.
11. The treatment process according to claim 6 , wherein the amount of the aqueous treatment solution added to the contaminated liquid is within a range of 1.0-5.0 ml/liter of the contaminated liquid.
12. The treatment process according to claim 6 , wherein the dispersing step involves at least one of: allowing the aqueous treatment solution to migrate and disperse through the contaminated liquid; heating the contaminated liquid; and mixing the treatment solution into the contaminated liquid.
13. The treatment process according to claim 6 , wherein collectively the at least one hydroxide compound and water constitute at least 98 weight percent of the aqueous treatment solution.
14. The treatment process according to claim 6 , wherein the collective concentration of the at least one hydroxide in the aqueous treatment solution is 45-55 weight percent.
15. The treatment process according to claim 6 , wherein the antibacterial agent includes at least one of a silicate compound and barium, and the antibacterial agent is added at a concentration of 0.1-2 weight percent in the aqueous treatment solution.
16. The treatment process according to claim 6 , wherein the aqueous treatment solution contains at least two different hydroxide compounds.
17. The treatment process according to claim 6 , wherein the amount of the aqueous treatment solution added to the contaminated liquid is within a range of 0.25-30.0 ml/liter of the contaminated liquid, and within said range the amount of the aqueous treatment solution added is based on whether it is desired to cause a precipitate containing sulfur is to be generated in the treated, contaminated liquid and a type of the precipitate containing sulfur desired to be generated.
18. The treatment process according to claim 17 , wherein when it is desired to cause a precipitate containing sulfur is to be generated in the treated, contaminated liquid the amount of the aqueous treatment solution added to the contaminated liquid is within a range of 6.0-30.0 ml/liter of the contaminated liquid.