Asphaltene inhibitors for squeeze applications

US9637676B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9637676-B2
Application numberUS-201313746441-A
CountryUS
Kind codeB2
Filing dateJan 22, 2013
Priority dateJan 24, 2012
Publication dateMay 2, 2017
Grant dateMay 2, 2017

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  5. First independent claim

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Abstract

Official abstract text for this publication.

Reaction products of polymeric alkyl phenol formaldehyde resins are useful as additives to inhibit or prevent the deposition or precipitation of asphaltenes in hydrocarbon fluids, particularly crude oil produced from a subterranean formation. These reaction products are formed by reacting a polymeric alkyl phenol formaldehyde resin with a co-reactant having functional groups including, but not necessarily limited to, amines, esters, silanes, ketones, epoxides, alkoxides, aryloxides, halogens, alkali metals, alkali earth metals, acetamides, non-metal oxides, metal oxides, where the co-reactant optionally has a carbon chain length between 1 and 22 and the reaction is conducted in the presence of at least one of various solvents. In one non-limiting embodiment, the co-reactant is a silicon derivative. The asphaltene inhibitors have utility when injected into a subterranean formation while oil production temporarily halts, a process called “squeezing,” because they are retained to a degree in the formation as the crude oil is produced.

First claim

Opening claim text (preview).

What is claimed is: 1. A method of inhibiting or preventing asphaltene deposition in a hydrocarbon fluid containing asphaltenes, the hydrocarbon fluid initially being within a subterranean formation, the method comprising: introducing to the hydrocarbon fluid from about 10 ppm to about 2000 ppm, based on the hydrocarbon fluid, independent of any water present, of asphaltene inhibitor effective to inhibit or prevent asphaltene deposition therein, where the asphaltene inhibitor comprises a reaction product of: an organic polymer which inhibits the precipitation of asphaltenes, where the organic polymer is selected from the group alkylphenol formaldehyde resins, alkylphenol formaldehyde amine resins, polyalkylsuccinic anhydrides, polyalkylsuccinic anhydride pentaerythritol condensate polymers, maleic anhydride alpha olefin polyesters, maleic anhydride fatty amine polyamides, sorbitan polyesters, alkyl polyacrylate esters, and combinations therein, with a co-reactant having functional groups selected from the group consisting of amines, esters, silanes, ketones, epoxides, alkoxides, aryloxides, halogens, alkali metals, alkali earth metals, acetamides, non-metal oxides, metal oxides and combinations thereof and where the co-reactant is one previously specified having a carbon chain length between 1 and 22 carbons; and adsorbing, crosslinking, or complexing the asphaltene inhibitor with reservoir rock of the subterranean formation in the presence of water. 2. The method of claim 1 , where the organic polymer is a polymeric alkylphenol formaldehyde resin. 3. The method of claim 2 where the polymeric alkylphenol formaldehyde resin may have a weight average molecular weight of from about 1000 to about 30,000 daltons. 4. The method of claim 1 where the co-reactant is a silicon derivative of the formula SiR 1 R 2 R 3 R 4 where each R n is independently selected from halogen, alkyl, O-alkyl, aryl, and O-aryl groups; where the alkyl groups are straight or branched and the alkyl groups and aryl groups may have from 1 to 22 carbon atoms. 5. The method of claim 1 where the organic polymer is a polymeric alkylphenol formaldehyde resin; and the co-reactant is a silicon derivative of the formula SiR 1 R 2 R 3 R 4 where each R n is independently selected from halogen, alkyl, O-alkyl, aryl, and O-aryl groups; where the alkyl groups are straight or branched and the alkyl groups and aryl groups may have from 1 to 22 carbon atoms. 6. The method of claim 5 where functional groups of the co-reactant take part in the reaction to a degree of from about 0.01 mole % to about 90 mole %. 7. The method of claim 1 where the asphaltene inhibitor is present in a solvent in a proportion of from about 10 wt % to about 90 wt %, the balance being a hydrophobic solvent selected from the group consisting of toluene, xylene, ethylbenzenes, aromatic naphthas, produced hydrocarbons, diesel, kerosene, unconventional solvents such as limonenes, turpentines, aliphatic hydrocarbons, polyethers, and combinations thereof. 8. The method of claim 1 where the hydrocarbon fluid is selected from the group consisting of crude oil and a combination of crude oil, formation brine, and hydrocarbon gases. 9. A method of inhibiting or preventing asphaltene deposition in a hydrocarbon fluid containing asphaltenes, the hydrocarbon fluid initially being within a subterranean formation, the method comprising: introducing from about 10 ppm to about 2000 ppm, based on the hydrocarbon fluid, independent of any water present, an asphaltene inhibitor into the subterranean formation, where the asphaltene inhibitor comprises a reaction product of: an organic polymer which inhibits the precipitation of asphaltenes, where the organic polymer is selected from the group alkylphenol formaldehyde resins, alkylphenol formaldehyde amine resins, polyalkylsuccinic anhydrides, polyalkylsuccinic anhydride pentaerythritol condensate polymers, maleic anhydride alpha olefin polyesters, maleic anhydride fatty amine polyamides, sorbitan polyesters, alkyl polyacrylate esters, and combinations therein, with a co-reactant having functional groups selected from the group consisting of amines, esters, silanes, ketones, epoxides, alkoxides, aryloxides, halogens, alkali metals, alkali earth metals, acetamides, non-metal oxides, metal oxides and combinations thereof and where the co-reactant is one previously specified having a carbon chain length between 1 and 22 carbons; and adsorbing, crosslinking, or complexing the asphaltene inhibitor with reservoir rock of the subterranean formation in the presence of water; further comprising after introducing the asphaltene inhibitor, subsequently introducing selected from the group consisting of: in the case that the subterranean formation produces a water cut of 1 vol % and greater, subsequently introducing an overflush of a hydrophobic solvent selected from the group consisting of toluene, xylene, ethylbenzenes, aromatic naphthas, produced hydrocarbons, diesel, kerosene, unconventional solvents such as limonenes, turpentines, aliphatic hydrocarbons or polyethers, and combinations thereof; and in the case that the subterranean formation produces a water cut of less than 1 vol %, subsequently introducing an overflush of water comprising from about 1 vol % to about 5 vol % of the asphaltene inhibitor previously injected into the formation followed by introducing a hydrophobic solvent selected from the group consisting of toluene, xylene, ethylbenzenes, aromatic naphthas, produced hydrocarbons, diesel, kerosene, unconventional solvents such as limonenes, turpentines, aliphatic hydrocarbons or polyethers, and combinations thereof. 10. The method of claim 9 further comprising, prior to introducing the asphaltene inhibitor, introducing a preflush chemical treatment into the subterranean formation, where the preflush fluids comprise about 0 to about 20 vol % of an asphaltene dispersant and the balance being a hydrophobic solvent selected from the group consisting of toluene, xylene, ethylbenzenes, aromatic naphthas, produced hydrocarbons, diesel, kerosene, unconventional solvents such as limonenes, turpentines, aliphatic hydrocarbons, polyethers, and combinations thereof. 11. The method of claim 9 where the co-reactant is a silicon derivative of the formula SiR 1 R 2 R 3 R 4 where each R n is independently selected from halogen, alkyl, O-alkyl, aryl, and O-aryl groups; where the alkyl groups are straight or branched and the alkyl groups and aryl groups may have from 1 to 22 carbon atoms. 12. The method of claim 11 where functional groups of the co-reactant takes part in the reaction to a degree of from about 0.01 mole % to about 90 mole %. 13. The method of claim 9 where water in the formation ranges in pH from about 1 to about 12.

Assignees

Inventors

Classifications

  • using chemical means for preventing or limiting {, e.g. eliminating,} the deposition of paraffins or like substances · CPC title

  • Chemically modified polycondensates · CPC title

  • C09K8/524Primary

    organic depositions, e.g. paraffins or asphaltenes · CPC title

  • Methods for stimulating production {(by vibrating earth formations E21B43/003)} · CPC title

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What does patent US9637676B2 cover?
Reaction products of polymeric alkyl phenol formaldehyde resins are useful as additives to inhibit or prevent the deposition or precipitation of asphaltenes in hydrocarbon fluids, particularly crude oil produced from a subterranean formation. These reaction products are formed by reacting a polymeric alkyl phenol formaldehyde resin with a co-reactant having functional groups including, but not …
Who is the assignee on this patent?
Leonard Geoffrey C, Rivers Gordon T, Asomaning Samuel, and 2 more
What technology area does this patent fall under?
Primary CPC classification C09K8/524. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue May 02 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).