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A process for removing a sulfur species from a stream selected from the group consisting of a hydrocarbon stream, an aqueous stream, and mixtures thereof is disclosed herein, which may include introducing a treating mixture into the stream. The treating mixture may include a compound of the general

A process for removing a sulfur species from a stream selected from the group consisting of a hydrocarbon stream, an aqueous stream, and mixtures thereof is disclosed herein, which may include introducing a treating mixture into the stream. The treating mixture may include a compound of the general formula selected from the group consisting of: or combinations of compound (I) or compound (II). R1 may be a C1-C30 hydrocarbyl group that is saturated, unsaturated, cyclic or branched, or may contain a heteroatom. ‘A’ may be an oxygen atom or a methylene group. R2 may be a C1-C30 hydrocarbyl group that may be saturated, unsaturated, cyclic or branched, or may contain a heteroatom(s) other than C and H. The treating mixture may reduce the reactive sulfur species in the stream. The sulfur species reduced from the stream may be hydrogen sulfide, mercaptans, polysulfides, or combinations thereof.

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1. A process for removing a sulfur species from a stream selected from the group consisting of a hydrocarbon stream, an aqueous stream, and mixtures thereof; which comprises introducing a treating mixture into the stream where the treating mixture comprises a compound of the general formula selected

1. A process for removing a sulfur species from a stream selected from the group consisting of a hydrocarbon stream, an aqueous stream, and mixtures thereof; which comprises introducing a treating mixture into the stream where the treating mixture comprises a compound of the general formula selected from the group consisting of: where: R1 is a C1-C30 hydrocarbyl group that is saturated, unsaturated, cyclic or branched, or contains a heteroatom(s) other than C and H; where: R1 is as above,where A is an oxygen atom or a methylene group,where R2 is a C1-C30 hydrocarbyl group that is saturated, unsaturated, cyclic or branched, or contains a heteroatom(s) other than C and H;and combinations of compound (I) and compound (II). 2. The process of claim 1 where the treating mixture further comprises a compound of formula (III) where: R1 is as above, andR2 is as above. 3. The process of claim 1 where the treating mixture further comprises a solvent. 4. The process of claim 3 where the concentration of the solvent within the treating mixture is from about 1 to about 99 wt %. 5. The process of claim 3 where the solvent is an aromatic solvent. 6. The process of claim 3 where the concentration of the compound within the treating mixture is from about 1 to about 99 wt % of the treating mixture. 7. The process of claim 1 where the hydrocarbyl of the R1 group is selected from the class consisting of an alkyl or alkenyl group, an oxygenated ether linkage, or a hydrocarbyl group having a cyclic or an aromatic ring structure. 8. The process of claim 7 where the hydrocarbyl of the R1 group is an ethyl group, a methyl group, a polyethylene glycol group, or an ethoxylated alkylphenol group. 9. The process of claim 1 where the R2 hydrocarbyl group of compound (II) is selected from the class consisting of an alkyl group; an alkenyl group; a hydrocarbyl group having an oxygen, a phosphorous, or another heteroatom; or a hydrocarbyl group that contains a cyclic or an aromatic structure. 10. The process of claim 9 where the R2 hydrocarbyl group of the compound (II) is an isopropyl group, an ethanol, or a phenyl group. 11. The process of claim 1 where the sulfur species is selected from the group consisting of hydrogen sulfide, mercaptans, polysulfides, and combinations thereof. 12. The process of claim 1 where the amount of the sulfur species in the stream is reduced to about 200 ppmv or below. 13. The process of claim 1 where the amount of the treating mixture is introduced into the stream in the range of from about 1 ppmv to about 50,000 ppmv. 14. The process of claim 13 where the amount of the compound within the treating mixture is introduced into the stream in the range of from about 50 ppmv to about 5,000 ppmv. 15. A process for removing a sulfur species from a stream selected from the group consisting of a hydrocarbon stream, an aqueous stream, and mixtures thereof; which comprises introducing a treating mixture into a stream where the treating mixture comprises a compound of the general formula selected from the group consisting of: where: R1 is a C1-C30 hydrocarbyl group that is saturated, unsaturated, cyclic or branched, or contains a heteroatom(s) other than C and H; where: R1 is as above,where A is an oxygen atom or a methylene group,where R2 is a C1-C30 hydrocarbyl group that is saturated, unsaturated, cyclic or branched, or contains a heteroatom(s) other than C and H;and combinations of compound (I) and compound (II); andwhere the amount of the sulfur species in the stream is reduced to about 200 ppmv or below; and where the amount of the treating mixture is introduced into the stream in the range of from about 1 ppmv to about 50,000 ppmv. 16. The process of claim 15 where the treating mixture further comprises a compound of formula (III) where: R1 is as above, andR2 is as above. 17. The process of claim 15 further comprising another compound within the treating mixture selected from the group consisting of a hydrotriazine-based compound, a metal oxide based compound, a metal hydroxide based compound, an amine based compound, or mixtures thereof. 18. The process of claim 15 where the hydrocarbyl of the R1 group is selected from the class consisting of an alkyl or alkenyl group, an oxygenated ether linkage, or a hydrocarbyl group having a cyclic or an aromatic ring structure. 19. The process of claim 15 where the R2 hydrocarbyl group of compound (II) is selected from the class consisting of an alkyl group; an alkenyl group; a hydrocarbyl group having an oxygen, a phosphorous, or another heteroatom; or a hydrocarbyl group that contains a cyclic or an aromatic structure. 20. The process of claim 15 where the amount of the compound within the treating mixture is introduced into the stream in the range of from about 50 ppmv to about 5,000 ppmv.