Emulsifiers for wellbore strengthening
US-2017174975-A1 · Jun 22, 2017 · US
US11535786B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11535786-B2 |
| Application number | US-201917309267-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 12, 2019 |
| Priority date | Nov 14, 2018 |
| Publication date | Dec 27, 2022 |
| Grant date | Dec 27, 2022 |
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A wellbore fluid may include an oleaginous fluid forming a continuous phase; a non-oleaginous fluid forming a discontinuous phase; at least one emulsifier stabilizing an emulsion of the non-oleaginous continuous phase within the oleaginous continuous phase; and at least one viscosifier dispersed into the oleaginous continuous phase in a concentration of at least 4 ppb; wherein upon subjecting the wellbore fluid to shear rate of at least 10,000 s −1 , the emulsion is disrupted and the non-oleaginous fluid contacts the at least one viscosifier, thereby solidifying the wellbore fluid.
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What is claimed: 1. A wellbore fluid comprising: an oleaginous fluid forming a continuous phase; a non-oleaginous fluid forming a discontinuous phase; at least one emulsifier stabilizing an emulsion of the non-oleaginous continuous phase within the oleaginous continuous phase; at least one viscosifier dispersed into the oleaginous continuous phase in a concentration of at least 4 ppb; and at least one crosslinker selected from the group consisting of a zirconium salt or an iron salt to crosslink the viscosifier dispersed in the oleaginous continuous phase, wherein upon subjecting the wellbore fluid to shear rate of at least 10,000 s −1 , the emulsion is disrupted and the non-oleaginous fluid contacts the at least one viscosifier, thereby solidifying the wellbore fluid; wherein the wellbore fluid comprises at least one hydratable non-organophillic clay present in a concentration that ranges from 10 pp to 20 ppb. 2. The wellbore fluid of claim 1 , wherein the oleaginous continuous phase is present in at least 20% by volume of the wellbore fluid. 3. The wellbore fluid of claim 1 , wherein the non-oleaginous discontinuous phase is present in at least 70% by volume of the wellbore fluid. 4. The wellbore fluid of claim 1 , wherein the at least one viscosifier is selected from the group of polysaccharides. 5. The wellbore fluid of claim 1 , wherein the at least one crosslinker is present in an amount less than 1 ppb. 6. The wellbore fluid of claim 1 , wherein the hydratable clay is dispersed in the oleaginous continuous phase. 7. The wellbore fluid of claim 1 , wherein the emulsifier is an imidazoline-derivative. 8. The wellbore fluid of claim 7 , wherein the emulsifier is selected from the group of hydroxyethyl imidazolines, aminoethyl imidazolines, amidoethyl imidazolines, alkylamphodiacetates, alkyliminipropionates, or alkylamphopropionates. 9. A method of reducing loss of a wellbore fluid in a wellbore to a formation, the method comprising: pumping a wellbore fluid into the wellbore, the wellbore fluid comprising: an oleaginous fluid forming a continuous phase; a non-oleaginous fluid forming a discontinuous phase; at least one emulsifier stabilizing an emulsion of the non-oleaginous continuous phase within the oleaginous continuous phase; and at least one viscosifier dispersed into the oleaginous continuous phase in a concentration of at least 4 ppb; subjecting the wellbore fluid to shear forces generated by pumping the wellbore fluid into the formation through a nozzle in a drill bit, thereby exposing the at least one viscosifier to the non-oleaginous fluid, wherein the wellbore near the drill bit is at a temperature of at least 65.6° C.; and allowing the wellbore fluid to solidify; wherein the wellbore fluid comprises at least one hydratable non-organophillic clay present in a concentration that ranges from 10 pp to 20 ppb. 10. The method of claim 9 , further comprising pumping the wellbore fluid into a circulation zone, wherein the wellbore fluid solidifies to form a seal or a plug at an entrance of a fracture, fissure or vug or inside a fracture, fissure or vug, thereby reducing a loss circulation. 11. The method of claim 9 , wherein the at least one viscosifier is selected from the group of polysaccharides. 12. The method of claim 9 , wherein the at least one hydratable clay is dispersed in the oleaginous continuous phase. 13. The method of claim 9 , wherein the wellbore fluid further comprises at least one crosslinker to crosslink the at least one viscosifier dispersed in the oleaginous continuous phase. 14. The method of claim 13 , wherein the at least one crosslinker is selected from the group consisting of a zirconium salt and an iron salt. 15. The method of claim 13 , wherein the at least one crosslinker is present in an amount less than 1 ppb. 16. The method of claim 9 , wherein the at least one emulsifier is an imidazoline-derivative.
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