Demulsification of a crude oil middle phase emulsion

Claim 2

A process for the demulsification of a middle phase emulsion of a crude oil emulsion produced by a surfactant flood comprising contacting the middle phase emulsion with a water-soluble alkali metal hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide in an amount sufficient to cause demulsification of the emulsion.

Claim 3

The process of claim 1 wherein the hydroxide is utilized in an amount of from about 0.05 to about 5.0 weight percent based on volume of the emulsion being treated.

Claim 4

The process of claim 1 wherein the hydroxide is added in an amount sufficient to obtain a pH of at least about 10.

Claim 5

The process of claim 3 wherein water is added in an amount equivalent to at least about 50 volume percent based on volume of the original emulsion.

Claim 6

The process of claim 1 wherein an additive selected from the group consisting of hydrogen peroxide and a tetraalkylammonium salt having at least one alkyl group containing 1-25 carbon atoms, is added in an amount sufficient to accelerate the rate of separation of the emulsion.

Claim 7

A process for the demulsification of a middle phase emulsion of a surfactant produced crude emulsion comprising contacting the middle phase emulsion with from about 0.05 to about 5.0 weight percent of a hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide, diluting the mixture with at least about 50 volume percent water, based on volume of original emulsion, and heating the mixture to a temperature of from about 75° F. (24° C.) to about 400° F. (204° C.) for a sufficient time to cause the emulsion to separate into at least two phases, one of which is an oil phase and separating the oil phase.

Claim 8

A process for the demulsification of a middle phase emulsion of a surfactant produced crude emulsion comprising contacting the middle phase emulsion with from about 0.05 to about 5.0 weight percent of a hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide, diluting the mixture with at least about 50 volume percent water, based on volume of original emulsion, and heating the mixture to a temperature of from about 75° F. (24° C.) to about 400° F. (204° C.) for a sufficient time to cause the emulsion to separate into at least two phases, one of which is an oil phase and separating the oil phase.

Claim 9

The process of claim 6 wherein the oil phase is separated and is thereafter contacted with an acid selected from the group consisting of a carboxylic acid selected from the group consisting of tartaric, mucic, citric, ethylenediaminetetraacetic, nitrilotriacetic, gluconic, lactic, glycolic and acetic acid; amine salts of said carboxylic acids; sulfuric acid and phosphoric acid in an amount sufficient to obtain a pH of less than about 8 and allowing the mixture to separate into at least two phases, one of which is an oil phase and separating the oil phase.

Claim 10

A process for the demulsification of a middle phase emulsion of a surfactant produced crude oil emulsion comprising: (a) contacting the middle phase emulsion with a water-soluble alkali metal hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide in an amount of from about 0.05 to about 5 weight percent based on volume of the middle phase emulsion and allowing the mixture to separate into phases one of which is an oil phase; (b) separating the oil phase; (c) contacting the oil phase with an acid selected from the group consisting of a carboxylic acid selected from the group consisting of tartaric, mucic, citric, ethylenediaminetetraacetic, nitrilotriacetic, gluconic, lactic, glycolic and acetic acid; amine salts of said carboxylic acids; sulfuric acid and phosphoric acid in an amount sufficient to obtain a pH of less than about 8 and allowing the mixture to separate into at least two phases, one of which is an oil phase; and (d) separating the oil phase of step (c).

Claim 11

A process for the demulsification of a middle phase emulsion of a surfactant produced crude oil emulsion comprising: (a) contacting the middle phase emulsion with a water-soluble alkali metal hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide in an amount of from about 0.05 to about 5 weight percent based on volume of the middle phase emulsion and allowing the mixture to separate into phases one of which is an oil phase; (b) separating the oil phase; (c) contacting the oil phase with an acid selected from the group consisting of a carboxylic acid selected from the group consisting of tartaric, mucic, citric, ethylenediaminetetraacetic, nitrilotriacetic, gluconic, lactic, glycolic and acetic acid; amine salts of said carboxylic acids; sulfuric acid and phosphoric acid in an amount sufficient to obtain a pH of less than about 8 and allowing the mixture to separate into at least two phases, one of which is an oil phase; and (d) separating the oil phase of step (c).

Claim 12

A process for the demulsification of a middle phase emulsion of a crude oil produced by a surfactant flood comprising: (a) contacting the middle phase emulsion with a water-soluble metal hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide in an amount of from about 0.05 to about 5 weight percent based on volume of middle phase emulsions; (b) heating the mixture of step (a) to a temperature of from about 75° F. to about 400° F. and allowing the mixture to separate into phases wherein one of the phases is an oil phase; (c) separating the oil phase; (d) contacting the oil phase of step (c) with an acid selected from the group consisting of a carboxylic acid selected from the group consisting of tartaric, mucic, citric, ethylenediaminetetraacetic, nitrilotriacetic, gluconic, lactic, glycolic and acetic acid and amine salts of said carboxylic acids; sulfuric and phosphoric acid in order to obtain a pH of less than about 8 and allowing the mixture to separate into phases wherein one phase is an oil phase; and (e) separating the oil phase from the mixture of step (d).

Claim 13

A process for the demulsification of a middle phase emulsion of a crude oil produced by a surfactant flood comprising: (a) contacting the middle phase emulsion with a water-soluble metal hydroxide selected from the group consisting of sodium hydroxide and potassium hydroxide in an amount of from about 0.05 to about 5 weight percent based on volume of middle phase emulsions; (b) heating the mixture of step (a) to a temperature of from about 75° F. to about 400° F. and allowing the mixture to separate into phases wherein one of the phases is an oil phase; (c) separating the oil phase; (d) contacting the oil phase of step (c) with an acid selected from the group consisting of a carboxylic acid selected from the group consisting of tartaric, mucic, citric, ethylenediaminetetraacetic, nitrilotriacetic, gluconic, lactic, glycolic and acetic acid and amine salts of said carboxylic acids; sulfuric and phosphoric acid in order to obtain a pH of less than about 8 and allowing the mixture to separate into phases wherein one phase is an oil phase; and (e) separating the oil phase from the mixture of step (d).

Claim 14

The process of claim 8 or 9 wherein the amine salt of a carboxylic acid is obtained by reacting said carboxylic acid, either prior to or concurrently with contacting the acid with the oil phase, with an amine selected from the group consisting of monoethanolamine, diethanolamine, triethanolamine, morpholine and polyalkyloxyamines having an average molecular weight of from about 200 to about 3500 and having the formula: R.sub.1 --(OA.sub.1).sub.p.sbsb.i OA.sub.2 N].sbsb.n wherein: R 1 is selected from the group consisting of hydrogen, an alkyl, an aryl, an alkylaryl, a heterocyclic and N,N' diurea; --OA 1 -- is an alkyleneoxy substituent; OA 2 N is a nitrogen-containing alkyleneoxy group; n is an integer having a value of at least 1 which denotes the number of OA 1 OA 2 N groups attached to R 1 ; p is 0 an integer denoting the number of --OA 1 -- units in each of the n groups attached to R 1 ; and i is a subscript which distinguishes between the individual p groups of each of the n groups.

Claim 15

The process of claim 10 wherein the oil following demulsification with the carboxylic acid or an amine salt of a carboxylic acid is acidic, and the oil phase is thereafter treated with a water-soluble amine of claim 10 and water in order to obtain a pH of between about 6 and about 9.

Claim 16

The process of claim 10 wherein the polyalkyloxyamine has an R 1 selected from the group consisting of 1,1,1-trimethylene propane, 1,1,1,1-tetramethylene methane, 1,2-propenyl, 1,2-ethenyl and N,N'-diurea; wherein --OA 1 -- and --OA 2 -- are each selected from the group consisting of an ethyleneoxy, propyleneoxy and butyleneoxy; and N is a nitrogen-containing substituent selected from the group consisting of amine, methylamine, dimethylamine, cyanoethylamine, hydroxyethylamine, morpholine, imidazole and ureide; wherein n has a value of 1 to 4 and wherein the average number of --OA 1 -- groups is from 0 to about 25 and has an average moleclar weight of from about 200 to about 3500.

Claim 17

The process of claim 11 wherein the water-soluble amine has demulsification properties and is a polyalkyloxyamine wherein the polyalkyloxyamine has an R 1 selected from the group consisting of 1,1,1-trimethylene propane, 1,1,1,1-tetramethylene methane, 1,2-propenyl, 1,2-ethenyl and N,N'-diurea; wherein --OA 1 -- and --OA 2 -- are each selected from the group consisting of an ethyleneoxy, propyleneoxy and butyleneoxy; and N is a nitrogen-containing substituent selected from the group consisting of amine, methylamine, dimethylamine, cyanoethylamine, hydroxyethylamine, morpholine, imidazole and ureide; wherein n has a value of 1 to 4 and wherein the average number of --OA 1 -- groups is from 0 to about 25 and has an average molecular weight of from about 200 to about 3500.

Claim 18

The process of claim 12 wherein the carboxylic acid is citric acid.

Claim 19

The process of claim 13 wherein R 1 is 1,1,1-trimethylene methane, --OA 1 -- and --OA 2 -- are each 2-propyleneoxy, N is a nitrogen-containing substituent which is a secondary amine, n is 3, the average number of --OA 1 -- groups in the polyalkyloxyamine is from about 0.75 to about 2.5 and the average molecular weight of the polyalkyloxyamine is from about 200 to about 400.