Biological decontamination gel and method for decontaminating surfaces by using this gel
US-9451765-B2 · Sep 27, 2016 · US
US11739246B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11739246-B2 |
| Application number | US-201917254884-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 1, 2019 |
| Priority date | Jun 29, 2018 |
| Publication date | Aug 29, 2023 |
| Grant date | Aug 29, 2023 |
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A method of recycling a direct emulsion wellbore fluid may include disrupting a direct emulsion comprising an aqueous external phase and an oleaginous internal phase, wherein the direct emulsion is stabilized by a surfactant composition; and separating the aqueous phase and the oleaginous phase.
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What is claimed: 1. A method of recycling a direct emulsion wellbore fluid, the method comprising: disrupting a direct emulsion comprising an aqueous external phase and an oleaginous internal phase, wherein the direct emulsion is stabilized by a surfactant composition; and separating the aqueous phase and the oleaginous phase; wherein disrupting the direct emulsion comprises adding an invert emulsifier; further comprising: formulating an invert emulsion wellbore fluid from the oleaginous phase comprising the invert emulsifier. 2. The method of claim 1 , wherein the surfactant composition comprises a phospholipid surfactant. 3. The method of claim 1 , wherein the separated oleaginous phase comprises less than 1 vol % of aqueous impurities. 4. The method of claim 1 , wherein disrupting the direct emulsion comprises increasing the pH of the direct emulsion to a pH equal to or greater than 10. 5. The method of claim 4 , further comprising neutralizing the aqueous phase prior to reuse. 6. The method of claim 1 , wherein the separated oleaginous phase is used to formulate a direct emulsion wellbore fluid. 7. The method of claim 1 , wherein the separated oleaginous phase is used to formulate an invert emulsion wellbore fluid. 8. The method of claim 1 , wherein the separated oleaginous phase comprises the invert emulsifier. 9. The method of claim 2 , wherein the phospholipid surfactant has the general formula: where R and R′ are C 6 to C 25 hydrocarbon groups and A is any suitable anion. 10. The method of claim 1 , wherein the surfactant composition further comprises a viscosifying agent. 11. The method of claim 1 , wherein the amount of oleaginous internal phase is from about 15% to about 50% by volume of the fluid. 12. The method of claim 1 , wherein the amount of aqueous external phase is from about 50% to about 85% by volume of the wellbore fluid.
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