Water-based formulation of H2S/mercaptan scavenger for fluids in oilfield and refinery applications

Patent metadata

Field	Value
Publication number	US-9708547-B2
Application number	US-201113172370-A
Country	US
Kind code	B2
Filing date	Jun 29, 2011
Priority date	Oct 15, 2007
Publication date	Jul 18, 2017
Grant date	Jul 18, 2017

Abstract

Hydrogen sulfide (H 2 S) and/or mercaptan scavengers are chemicals that remove H 2 S and/or mercaptans from gas, oil and water. Water-based formulations may be made and used employing scavenging compounds having the formulae:

wherein each R 1 , R 2 , R 3 , and R 4 are the same or different and are selected from the group consisting of hydrogen, an alkyl, an alkenyl, an aryl, an acyl, a halogen, a hydroxyl, a nitro, an alkyl ester, an aryl ester, an alkyl ether, an aryl ether, a hydroxymethyl, an anhydride group, an amino, and a sulfide. In one non-limiting embodiment the compounds (A) and (B) do not contain nitrogen atoms. Water-based formulations, such as those using a protic solvent with the above compounds, work well as H 2 S scavengers.

First claim

What is claimed is:

1. A method for scavenging hydrogen sulfide from a fluid comprising: contacting the fluid with an effective amount of a protic composition to reduce the amount of hydrogen sulfide as compared to an identical method absent the protic composition, the protic composition consisting of:
a protic solvent;
optionally a base selected from the group consisting of sodium hydroxide, potassium hydroxide and combinations thereof; and
a non-nitrogen-based compound having a formula selected from the group consisting of:

wherein each R 1 , R 2 , R 3 , and R 4 are the same or different and are selected from the group consisting of hydrogen, an alkyl, an alkenyl, an aryl, an acyl, a halogen, a hydroxyl, an alkyl ester, an aryl ester, an alkyl ether, an aryl ether, a hydroxymethyl, an anhydride, and a sulfide, and where the fluid is selected from the group consisting of:
an aqueous phase,
a gaseous phase,
a mixture of an aqueous phase and a gaseous phase,
a mixture of an aqueous phase and a hydrocarbon phase, and
a mixture of an aqueous phase, a gaseous phase and a hydrocarbon phase.

2. The method of claim 1 where the protic composition has a pH of greater than 9.

3. The method of claim 1 where the protic composition has a pH of from about 11 to about 13.

4. The method of claim 1 where the base is present at a concentration effective to give the composition a pH of greater than 9.

5. The method of claim 1 where the method scavenges H 2 S from a fluid selected from the group consisting of an aqueous phase and mixtures of an aqueous phase and a hydrocarbon phase and the compound is present in the protic composition at a concentration of from about 50 to about 1000 ppm by mass.

6. The method of claim 5 where the method is practiced in a refinery.

7. The method of claim 1 where the method scavenges H 2 S from a gaseous phase and the method is practiced by a process selected from the group consisting of:
contacting the gaseous phase with droplets of the protic composition; and
passing the gaseous phase through the protic composition, where the compound is present in the protic composition in a concentration of at least 50 vol%.

8. A method for scavenging hydrogen sulfide from a fluid comprising: contacting the fluid with from about 50 weight % to about 99 weight % of a protic composition to reduce the amount of hydrogen sulfide therein, the protic composition consisting of:
a protic solvent;
optionally a base selected from the group consisting of sodium hydroxide, potassium hydroxide and combinations thereof; and
a non-nitrogen-based compound having a formula selected from the group consisting of:

wherein each R 1 , R 2 , R 3 , and R 4 are the same or different and are selected from the group consisting of hydrogen, an alkyl, an alkenyl, an aryl, an acyl, a halogen, a hydroxyl, an alkyl ester, an aryl ester, an alkyl ether, an aryl ether, a hydroxymethyl, an anhydride, and a sulfide where the protic composition has a pH of greater than 9 and the protic composition contains at least about 50 ppm by mass of the compound, and where the fluid is selected from the group consisting of:
an aqueous phase,
a gaseous phase,
a mixture of an aqueous phase and a gaseous phase,
a mixture of an aqueous phase and a hydrocarbon phase, and
a mixture of an aqueous phase, a gaseous phase and a hydrocarbon phase.

9. The method of claim 8 where the composition has a pH of from about 11 to about 13.

10. The method of claim 8 where the base is present at a concentration effective to give the composition a pH of greater than 9.

11. The method of claim 8 where the method scavenges H 2 S from a fluid selected from the group consisting of an aqueous phase and mixtures of an aqueous phase and a hydrocarbon phase.

12. The method of claim 11 where the method is practiced in a refinery.

13. The method of claim 8 where the method scavenges H 2 S from a gaseous phase and the method is practiced by a process selected from the group consisting of:
contacting the gaseous phase with droplets of the protic composition; and
passing the gaseous phase through the protic composition, where the compound is present in the protic composition in a concentration of at least 50 vol %.

14. A method for scavenging hydrogen sulfide from a fluid consisting of: contacting the fluid with from about 50weight % to about 99 weight % of a protic composition to reduce the amount of hydrogen sulfide therein, the protic composition consisting of:
a protic solvent;
a base selected from the group consisting of sodium hydroxide, potassium hydroxide and combinations thereof; and
a non-nitrogen-based compound having a formula selected from the group consisting of:

wherein each R 1 , R 2 , R 3 , and R 4 are the same or different and are selected from the group consisting of hydrogen, an alkyl, an alkenyl, an aryl, an acyl, a halogen, a hydroxyl, an alkyl ester, an aryl ester, an alkyl ether, an aryl ether, a hydroxymethyl, an anhydride, and a sulfide where the protic composition has a pH of from about 11 to about 13 and the protic composition contains at least about 50 ppm by mass of the compound, and where the fluid is selected from the group consisting of:
an aqueous phase,
a gaseous phase,
a mixture of an aqueous phase and a gaseous phase,
a mixture of an aqueous phase and a hydrocarbon phase, and
a mixture of an aqueous phase, a gaseous phase and a hydrocarbon phase.

15. The method of claim 14 where the method scavenges H 2 S from a fluid selected from the group consisting of an aqueous phase and mixtures of an aqueous phase and a hydrocarbon phase.

16. The method of claim 15 where the method is practiced in a refinery.

17. The method of claim 14 where the method scavenges H 2 S from a gaseous phase and the method is practiced by a process selected from the group consisting of:
contacting the gaseous phase with droplets of the protic composition; and
passing the gaseous phase through the protic composition, where the compound is present in the protic composition in a concentration of at least 50 vol %.

Assignees

• Ramachandran Sunder
• Jovancicevic Vladimir
• Tsang Ying H
• Squicciarini Michael P
• Prince Philippe
• Yang Jianzhong
• Cattanach Kyle C
• Baker Hughes Inc

Inventors

• Ramachandran Sunder
• Jovancicevic Vladimir
• Tsang Ying H
• Squicciarini Michael P
• Prince Philippe
• Yang Jianzhong
• Cattanach Kyle C

Classifications

• C10G19/02

  with aqueous alkaline solutions · CPC title

• B01D2252/103

  Water · CPC title

• B01D53/1487

  Removing organic compounds · CPC title

• C10G19/04

  containing solubilisers, e.g. solutisers · CPC title

• B01D2257/304

  Hydrogen sulfide · CPC title