Recycling of oil-based drilling muds
View Patent ↗A method of recovering hydrocarbon or synthetic base oils from used oil-based drilling mud utilizes acid to deactivate emulsifiers in the drilling mud for altering the emulsion stability and permitting removal of the solids contained in the drilling mud using conventional separation such as centrifugation. A surfactant is typically added to prevent water-wetting as a result of the addition of the acid. The recovered base oil contains substantially all of the deactivated emulsifiers, which can be reactivated through the addition of lime, allowing new drilling fluids to be prepared without the need to add significant amounts of emulsifier to the recycled base oil.
1. A method for recycling a used, water-in-oil emulsion drilling mud comprising fatty acid emulsifiers or derivatives thereof, the method comprising:
adding an acid to the used mud sufficient to reduce the pH of a water phase to a value less than 7 for deactivating the fatty acid emulsifiers or derivatives thereof in the drilling mud, the acid selected for having low affinity for an oil phase of the drilling mud;
mixing the drilling mud with the acid for sufficient time to deactivate the fatty acid emulsifiers or derivatives thereof;
separating the treated drilling mud for separating the base oil phase from the water phase and from solids, including ultra-fine solids and organoclays, contained therein, the recovered base oil phase containing at least substantially all of the deactivated fatty acid emulsifiers or derivatives thereof; and
adding lime to the recovered base oil phase for reactivating the fatty acid emulsifiers or derivatives thereof contained therein for use in preparing a new drilling mud without the need to add additional fatty acid emulsifiers or derivatives thereof.
2. The method of claim 1 further comprising prior to adding the acid:
adding a surfactant, the amount of surfactant being sufficient to prevent viscosity increases as a result of water-wetting of the organoclays in the used drilling mud; and
mixing the surfactant with the used drilling mud.
3. The method of claim 2 wherein the surfactant is an anionic surfactant.
4. The method of claim 2 wherein the surfactant is dodecyl benzene sulphonic acid (DDBSA).
5. The method of claim 4 wherein the DDBSA is added in an amount from 0% to about 10% by volume.
6. The method of claim 4 wherein the DDBSA is added in an amount from 0% to about 3% by volume.
7. The method of claim 1 wherein the separating is by centrifugation.
8. The method of claim 1 wherein the acid further comprises a non-emulsifier, the amount of the non-emulsifier being sufficient to prevent the acid from forming an oil-in-water or an oil-in-water-in-oil emulsion in the drilling mud.
9. The method of claim 8 wherein the non-emulsifier is added in amount from 0% to about 10% by weight.
10. The method of claim 8 wherein the non-emulsifier is added in amount from 0% to about 3% by weight.
11. The method of claim 8 wherein the non-emulsifier is selected to be soluble in the acid and to remain substantially in the water phase.
12. The method of claim 1 wherein the acid is a mineral acid.
13. The method of claim 12 wherein the acid is hydrochloric acid added in a range of from about 1 volume % to about 99 volume %.
14. The method of claim 12 wherein the acid is hydrochloric acid added in a range of from about 5 volume % to about 60 volume %.
15. The method of claim 1 wherein the acid further comprises a corrosion inhibitor.
16. The method of claim 1 wherein the lime is added in an amount sufficient to achieve desired emulsion stability.
17. The method of claim 8 wherein the non-emulsifier is a mixture of polyalkylene glycols.
18. The method of claim 15 wherein the corrosion inhibitor is soluble in the acid.