Additives to enhance phosphorus compound removal in refinery desalting processes
View Patent ↗Reactive phosphorus species can be removed or transferred from a hydrocarbon phase to a water phase in an emulsion breaking process by using a composition that contains water-soluble hydroxyacids. Suitable water-soluble hydroxyacids include, but are not necessarily limited to glycolic acid, gluconic acid, C 2 -C 4 alpha-hydroxy acids, poly-hydroxy carboxylic acids, thioglycolic acid, chloroacetic acid, polymeric forms of the above hydroxyacids, poly-glycolic esters, glycolate ethers, and ammonium salt and alkali metal salts of these hydroxyacids, and mixtures thereof. The composition may optionally include a mineral acid to reduce the pH of the desalter wash water. A solvent may be optionally included in the composition. The invention permits transfer of reactive phosphorus species into the aqueous phase with little or no hydrocarbon phase undercarry into the aqueous phase. The composition is particularly useful in treating crude oil emulsions, and in removing calcium and other metals therefrom.
1. A method of transferring reactive phosphorus species from a hydrocarbon phase to a water phase in a refinery desalting process comprising:
adding to wash water, an effective amount of a composition to transfer at least a portion of the reactive phosphorus species from a hydrocarbon phase to a water phase, the composition comprising at least one water-soluble hydroxyacid selected from the group consisting of gluconic acid, C 2 -C 4 alpha-hydroxy acids, poly-hydroxy carboxylic acids, thioglycolic acid, chloroacetic acid, polymeric forms of the above hydroxyacids, poly-glycolic esters, glycolate ethers, and ammonium salt and alkali metal salts of these hydroxyacids, and mixtures thereof;
adding the wash water to hydrocarbon to create an emulsion; and
resolving the emulsion into hydrocarbon phase and an aqueous phase using electrostatic coalescence, where at least a portion of the reactive phosphorus species is transferred to the aqueous phase.
2. The method of claim 1 where in the adding of the composition, the composition additionally comprises a mineral acid.
3. The method of claim 2 where in the adding of the composition, the composition further comprises
down to about 1 wt. % water-soluble hydroxyacid; and
up to about 20 wt. % mineral acid.
4. The method of claim 2 where the amount of mineral acid is sufficient to lower the pH of the wash water to 6 or below.
5. The method of claim 1 where in the adding of the composition, the water-soluble hydroxyacid is present in the emulsion in an amount ranging from about 1 about 10,000 ppm.
6. The method of claim 1 where in the adding of the composition, the composition further comprises water or alcohol solvent.
7. The method of claim 1 further comprising after adding the composition to the emulsion, heating the emulsion to a temperature above about 180° F. (about 82° C.).
8. A method of transferring reactive phosphorus species from a hydrocarbon phase to a water phase in a refinery desalting process comprising:
adding to wash water, an effective amount of a composition to transfer at least a portion of the reactive phosphorus species from a hydrocarbon phase to a water phase, the composition comprising a mineral acid and at least one water-soluble hydroxyacid selected from the group consisting of gluconic acid, C 2 -C 4 alpha-hydroxy acids, poly-hydroxy carboxylic acids, thioglycolic acid, chloroacetic acid, polymeric forms of the above hydroxyacids, poly-glycolic esters, glycolate ethers, and ammonium salt and alkali metal salts of these hydroxyacids, and mixtures thereof, where the water-soluble hydroxyacid comprises from about 1 to about 100 wt. % of the composition and the composition further comprises a water or alcohol solvent;
adding the wash water to hydrocarbon to create an emulsion and
resolving the emulsion into hydrocarbon phase and an aqueous phase using electrostatic coalescence, where at least a portion of the reactive phosphorus species is transferred to the aqueous phase.
9. The method of claim 8 where the amount of mineral acid is sufficient to lower the pH of the wash water to 6 or below.
10. The method of claim 8 further comprising after adding the composition to the emulsion, heating the emulsion to a temperature above about 180° F. (about 82° C.).
11. A treated hydrocarbon emulsion comprising:
a hydrocarbon phase;
a water phase;
a composition in an amount effective for transferring ay least a portion of a reactive phosphorus species from the hydrocarbon phase to the water phase, the composition comprising a water-soluble hydroxyacid selected from the group consisting of gluconic acid, C 2 -C 4 alpha-hydroxy acids, poly-hydroxy carboxylic acids, thioglycolic acid, chloroacetic acid, polymeric forms of the above hydroxyacids, poly-glycolic esters, glycolate ethers, and ammonium salt and alkali metal salts of these hydroxyacids, and mixtures thereof; and
a mineral acid.
12. The treated hydrocarbon emulsion of claim 11 where the composition further comprises:
down to about 1 wt. % water-soluble hydroxyacid; and
up to about 20 wt. % mineral acid.
13. The treated hydrocarbon emulsion of claim 11 further comprising wash water and where the amount of mineral acid is sufficient to lower the pH of the wash water to 6 or below.
14. The treated hydrocarbon emulsion of claim 11 where the water-soluble hydroxyacid is present in the emulsion in an amount ranging from about 1 to about 10,000 ppm.
15. The treated hydrocarbon emulsion of claim 11 where the composition further comprises at least one additional component selected from the group consisting of a water or alcohol solvent, a corrosion inhibitor, a demulsifier, a scale inhibitor, metal chelants, wetting agents and mixtures thereof.
16. The treated hydrocarbon emulsion of claim 11 where the hydrocarbon component contains more than 3 ppm of a reactive phosphorus species.