Advisory controls of desalter system
US-2015361350-A1 · Dec 17, 2015 · US
US9353261B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9353261-B2 |
| Application number | US-201213452222-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 20, 2012 |
| Priority date | Mar 27, 2012 |
| Publication date | May 31, 2016 |
| Grant date | May 31, 2016 |
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Disclosed and claimed is a microemulsion-based demulsifier composition and a method of demulsifying an emulsion comprising hydrocarbon and water. The demulsifier composition includes (i) an oil-like phase comprising at least one nonionic surfactant having a hydrophilic-lipophilic balance (HLB) of less than about 9; (ii) a coupling agent capable of stabilizing the demulsifier composition; (iii) at least one water-soluble or dispersible nonionic surfactant that is different from the at least one nonionic surfactant in the oil-like phase; (iv) at least one additional surfactant selected from anionic, cationic, amphoteric, and combinations thereof; (v) at least one nonionic demulsifier; and (vi) water.
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The claimed invention is: 1. A method of resolving an emulsion of water and crude petroleum oil, the method comprising: obtaining a crude petroleum oil from a subterranean reservoir; mixing the crude petroleum oil with a wash water, resulting in a water-in-crude oil emulsion; adding a demulsifier composition to the water-in-crude oil emulsion to form a treated emulsion, the demulsifier composition comprising: (i) a first nonionic surfactant having a hydrophilic-lipophilic balance (HLB) of less than about 9; (ii) a coupling agent capable of stabilizing the demulsifier composition in the amount of from about 5% to about 40% based on the total weight of the demulsifier composition; (iii) a second nonionic surfactant that is water-soluble or dispersible and is different from the first nonionic surfactant; (iv) at least one additional surfactant selected from the group consisting of anionic surfactants, cationic surfactants, amphoteric surfactants, and combinations thereof in the amount of from about 2% to about 20% based on the total weight of the demulsifier composition ; (v) at least one nonionic demulsifier comprising a polyethyleneimine alkoxylate, a cross-linked ethylene oxide/propylene oxide copolymer, or combinations thereof; and (vi) water; and separating the crude petroleum oil from the water. 2. The method of claim 1 wherein the adding is accomplished by injecting the demulsifier composition into a crude oil process stream between a well head and a final oil storage tank. 3. The method of claim 1 wherein the adding is accomplished continuously or in batch fashion. 4. The method of claim 1 , further comprising allowing the treated emulsion to stand in a quiescent state for a period of time sufficient to obtain separation of the treated emulsion into distinct layers of water and oil prior to the separating. 5. The method of claim 4 , wherein the allowing the treated emulsion to stand is accomplished in a settling tank. 6. The method of claim 1 wherein the amount of the demulsifier composition added to the water-in-crude oil emulsion is about 10 ppm to 5000 ppm based on the volume of crude oil production. 7. The method of claim 1 , wherein the at least one additional surfactant is selected from the group consisting of cationic, amphoteric, and combinations thereof. 8. The method of claim 1 , wherein the first nonionic surfactant having an HLB of less than about 9 comprises an alkoxylated alcohol, an alkoxylated alkylphenol, a glycerol ester, a glycol ester, a polyethyleneglycol ester, a polyglycerol ester, a sorbitol ester, an ethylene oxide/propylene oxide copolymer, or a combination thereof. 9. The method of claim 8 , wherein the alkoxylated alcohol is selected from the group consisting of ethoxylated and propoxylated C 6 -C 20 alcohols; and mixtures thereof. 10. The method of claim 9 , wherein said alkoxylated alcohol comprises about 1-6 moles of said alkylene oxide per mole of alcohol. 11. The method of claim 1 , wherein the amount of the first nonionic surfactant is about 0.1% to about 35% by weight based on the total weight of the demulsifier composition. 12. The method of claim 1 , wherein the amount of the first nonionic surfactant is about 2% to about 25% by weight based on the total weight of the demulsifier composition. 13. The method of claim 1 , wherein the coupling agent is a water-soluble organic solvent. 14. The method of claim 13 , wherein the water-soluble organic solvent is selected from the group consisting of short chain alcohols with between 1 and 6 carbon atoms; diols with between 1 and 6 carbon atoms; glycerol; alkyl ethers of alkylene glycols with between 1 and 6 carbon atoms; polyalkylene glycols less than 6 kD; and mixtures thereof. 15. The method of claim 1 , wherein from about 2% to about 30% of the at least one nonionic demulsifier is present, based on total weight. 16. The method of claim 1 , wherein the second nonionic surfactant includes an alkoxylated alcohol, ethylene oxide/propylene oxide copolymers, and/or alkoxylated alkylphenol having an HLB greater than about 10. 17. The method of claim 1 , wherein from about 2% to about 25% of the second nonionic surfactant is present, based on weight. 18. The method of claim 1 , wherein the at least one additional surfactant is selected from the group consisting of linear alkylbenzene sulfonic acid, alkyl benzene sulfonate, alkane sulfonate, alkyl sulfate, alkyl ether sulfate, alkyl ammonium halides, alkyl aryl ammonium halides, imidazolium, cocoamidopropyl betaine, cocodimethyl betaine, alkyl amine oxide, and combinations thereof exclusive of combinations with both anionic and cationic surfactants.
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