Inhibiting corrosion caused by aqueous aldehyde solutions
Aldehydes useful as H 2 S sulfide scavengers may be corrosive to some metals such as steel, iron and aluminum, but the corrosive effect of the aldehydes may be mitigated by employing a corrosion inhibitor selected from the group consisting of a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, a phosphate ester, a thiophosphate ester, a thioamine, a Mannich Reaction Product, and combinations thereof.
1. A method for employing an aldehyde selected from the group consisting of glyoxal, acrolein, glutaraldehyde, and combinations thereof, in an aqueous solution while mitigating corrosion of metal in contact with the aldehyde solution, the method comprising employing a corrosion inhibitor with the aldehyde wherein the corrosion inhibitor comprises a member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, a phosphate ester, a thiophosphate ester, a thioamine, a Mannich Reaction Product, and combinations thereof.
2. The method of claim 1 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof is selected from the group consisting of LiH 2 PO 4 , NaH 2 PO 4 , Na 2 HPO 4 , Na 3 PO 4 , KH 2 PO 4 , K 2 HPO 4 , K 3 PO 4 and combinations thereof.
3. The method of claim 1 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof includes more than one cation.
4. The method of claim 3 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof includes two or more cations selected from the group consisting of lithium, potassium, sodium and combinations thereof.
5. The method of claim 1 wherein the aqueous aldehyde solution has an aldehyde concentration of from about 4 to about 90 weight percent.
6. The method of claim 1 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof is present in the aqueous aldehyde solution at a concentration of from about 100 ppm to 30% (by wt.).
7. The method of claim 1 wherein the aldehyde and corrosion inhibitor solution is employed at a pH range of from about 5 to about 9.0.
8. The method of claim 1 , wherein the pH range may vary from about 4.5 to about 9.
9. A process for exploring for or producing crude oil and/or natural gas comprising employing a H 2 S sulfide scavenger solution comprising an aldehyde and employing a corrosion inhibitor in the solution comprising a member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, a phosphate ester, a thiophosphate ester, a thioamine, Mannich Reaction Product, and combinations thereof, wherein the aldehyde is selected from the group consisting of glyoxal, acrolein, glutaraldehyde, and combinations thereof.
10. The process of claim 9 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof is selected from the group consisting of LiH 2 PO 4 ; NaH 2 PO 4 , Na 2 HPO 4 ; Na 3 PO 4 ; KH 2 PO 4 , K 2 HPO 4 ; K 3 PO 4 ; and combinations thereof.
11. The process of claim 9 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof includes more than one cation.
12. The process of claim 11 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof includes two or more cations selected from the group consisting of lithium, potassium, sodium, and combinations thereof.
13. The process of claim 9 wherein the H 2 S sulfide scavenger solution has an aldehyde concentration of from about 4 to about 90 weight percent.
14. The process of claim 9 wherein the member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof is present in the H 2 S sulfide scavenger solution at a concentration of from about 100 ppm to 30% (by wt.).
15. The process of claim 9 wherein the H 2 S sulfide scavenger solution comprising aldehyde and member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, and combinations thereof, has a pH range of from about 4.0 to about 9.0.
16. The process of claim 15 , wherein the pH range may vary from about 5 to about 9.
17. The process of claim 9 wherein the H 2 S sulfide scavenger and corrosion inhibitor are atomized and injected into a gas stream.
18. The process of claim 9 wherein the H 2 S sulfide scavenger and corrosion inhibitor are admixed with crude oil.
19. The process of claim 9 wherein hydrogen sulfide is present in a gaseous stream and the hydrogen sulfide-containing stream is passed through a contact tower or bubble tower including the H 2 S sulfide scavenger solution comprising the aldehyde and employing a corrosion inhibitor in the solution comprising a member selected from the group consisting of a mono-basic soluble phosphate salt, a di-basic soluble phosphate salt, a tri-basic soluble phosphate salt, a phosphate ester, a thiophosphate ester, a thioamine and combinations thereof.