US4813482A
Expired / Lapsed
US
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Method for removal of paraffin from producing oil wells
Assignee: Rhone Poulenc Surfactants and Specialties LP
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Filing: 1987-09-17
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Granted: 1989-03-21
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Expires: 2007-09-17
Abstract
Abstract A method for removing paraffin from a producing oil well comprising (a) contacting a mixture of a paraffin-dispersing effective amount of an alkyl or aralkyl polyoxyalkylene phosphate ester surfactant in the free acid form, or in the form of the alkali metal, amine, or ammonium salt, a mutual solvent and water, said mixture having a temperature of from about 30° to 40° F. higher than the melting point of the paraffin to be removed, with the interior of the oil well for a period of time sufficient to disperse paraffin within the well into the mixture; and (b)removing the mixture and the paraffin dispersed therein from the interior of the well.
Inventors
- 👤 William B. Walton
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 14:26
CPC Classifications
C; C09; C09K; C09K8/00; C09K8/52; C09K8/524; E; E21; E21B; E21B43/00; E21B43/34; E21B43/40; E21B43/35; Y; Y10; Y10S; Y10S507/00; Y10S507/927; Y10S507/929; Y10S507/931
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
200 words
A method for removing paraffin from a producing oil well comprising the steps of: a. preparing a mixture of a paraffin-dispersing effective amount of an alkyl aralkyl polyoxyalkylene phosphate ester surfactant in the free acid form, or in the form of the alkali metal, amine, or ammonium salt; a mutual solvent composed of a blend of an alcohol selected from the group consisting of aliphatic alcohols, glycols, polyglycols and glycol esters and mixtures thereof and an aromatic hydrocarbon selected from the group consisting of benzene, toluene, and xylene, and water and heating said mixture to a temperature of from about 30° to 40° F. higher than the melting point of the paraffin to be removed to form a micelle wherein the micelle mixture contains from about 8 to 35 weight percent of the phosphate ester surfactant, from about 65 to 95 weight percent of the mutual solvent, and from about 70 to 90 weight percent of water; b. contacting said micelle mixture with the interior of the oil well for a period of time sufficient to disperse paraffin within the well into the mixture; and c. removing the mixture and the paraffin dispersed therein from the interior of the well.
Claim 2
Independent Claim
200 words
A method for removing paraffin from a producing oil well comprising the steps of: a. preparing a mixture of a paraffin-dispersing effective amount of an alkyl aralkyl polyoxyalkylene phosphate ester surfactant in the free acid form, or in the form of the alkali metal, amine, or ammonium salt; a mutual solvent composed of a blend of an alcohol selected from the group consisting of aliphatic alcohols, glycols, polyglycols and glycol esters and mixtures thereof and an aromatic hydrocarbon selected from the group consisting of benzene, toluene, and xylene, and water and heating said mixture to a temperature of from about 30° to 40° F. higher than the melting point of the paraffin to be removed to form a micelle wherein the micelle mixture contains from about 8 to 35 weight percent of the phosphate ester surfactant, from about 65 to 95 weight percent of the mutual solvent, and from about 70 to 90 weight percent of water; b. contacting said micelle mixture with the interior of the oil well for a period of time sufficient to disperse paraffin within the well into the mixture; and c. removing the mixture and the paraffin dispersed therein from the interior of the well.
Claim 3
Dependent Claim
59 words
The method of claim 1 wherein the phosphate ester surfactant and mutual solvent are first mixed together and then the water component at a temperature in the range from about 30° to 40° F. greater than the melting point of the paraffin to be removed is added to the first formed mixture to form the final heated micelle mixture
Claim 4
Dependent Claim
65 words
The method of claim 1 wherein the amount of phosphate ester surfactant is in the range of from about 15 to 20 weight percent, the amount of mutual solvent is in the range of from about 80 to 85 weight percent, and the amount of water is in the range of from 80 to 85 weight percent based on the weight of the total composition.
Claim 5
Dependent Claim
23 words
The method of claim 1 or 2 wherein the temperature of the mixture is in the range from about 160° to 180° F.
Claim 6
Dependent Claim
211 words
The method of claim 1 or 2 wherein the phosphate ester has the formula: ##STR6## wherein: R 1 represents an alkyl radical having 10 to 18 carbon atoms; R 2 represents an alkyl of about 5 to 27 carbon atoms cycloalkyl, and radicals derived from mineral oils containing alkyl, cycloalkyl and mixed alkylcycloalkyl radicals having from about 12 to 27 carbon atoms; R 3 and R 4 represent hydrogen, alkyl having from about 1 to 22 carbon atoms, cycloalkyl, and radicals derived from mineral oils containing alkyl, cycloalkyl and mixed alkylcycloalkyl radicals having from about 12 to 27 carbon atoms; A represents the residue of ethylene oxide, ethylene oxide and tetrahydrofuran, or mixed lower alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, and butylene oxide alone or including tetrahydrofuran; and wherein the total molecular weight of the ester is about 500 to about 1,500, and A is heteric or block in molecular configuration; and wherein the degree of oxyalkylation is represented by n; x and y are 1 or 2; the sum of x and y is 3; z is an integer from 0 to 5; and X is hydrogen or a monovalent cation selected from the group consisting of an alkali metals; alkyl amines and ammonium.
Claim 7
Dependent Claim
82 words
The process of claim 1 or 2 wherein the phosphate ester surfactant is selected from the group consisting of block copolymers of propylene glycol to which propylene oxide and then ethelyne oxide have been added; reverse block copolymers of ethylene glycol to which ethylene oxide and then propylene oxide have been added, tetrols of ethylenediamine to which propylene oxide and then ethylene oxide have been added, and reverse tetrols of ethylenediamine to which ethylene oxide and then propylene oxide have been added.
Claim 8
Dependent Claim
145 words
The process of claim 6 wherein the phosphate ester is selected from the group consisting of the reaction products of a phosphorus acid reactant with a diol or tetrol selected from the group consisting of: polyol diols having the formula ##STR7## wherein a, b, and c are integers chosen so that the molecular weight of the diol is from about 1,100 to 14,000; reverse polyol diols having the formula ##STR8## wherein b and n are chosen so that the molecular weight of the diol is from about 1,950 to 9,000; polyol tetrols having the formula ##STR9## wherein x and y are chosen so that the tetrol has a molecular weight from about 1,650 to about 26,000; and reverse polyol tetrols having the formula ##STR10## wherein x and y are chosed so that the tetrol has a molecular weight range of from about 2,700 to 16,000.
Claim 9
Dependent Claim
32 words
The process of claim 1 or 2 wherein the water contains an alkali metal salt in an amount from about 2 to 5 weight percent based on the weight of the water.
Claim 10
Independent Claim
267 words
A method for the recovery of paraffin solidified in producing oil wells in the form of usable hydrocarbon comprising the steps of: a. preparing a mixture of a paraffin-dispersing effective amount of an alkyl or aralkyl polyoxyalkylene phosphate ester surfactant in the free acid form, or in the form of the alkali metal, amine, or ammonium salt; a mutual solvent composed of a blend of an alcohol selected from the group consisting of aliphatic alcohols, glycols, polyglycols and glycol esters and mixtures thereof and an aromatic hydrocarbon selected from the group consisting of benzene, toluene, and xylene, and water, and heating said mixture to a temperature of from about 30° to 40° F. higher than the melting point of the paraffin to be removed to form a micelle, wherein the micelle mixture contains from about 8 to 35 weight percent of the phosphate ester surfactant, from about 65 to 95 weight percent of the mutual solvent, and from about 70 to 90 weight percent of water; b. contacting said micelle mixture with the interior of the oil well for a period of time sufficient to disperse paraffin within the well into the mixture; and c. removing the mixture and the paraffin dispersed therein from the interior of the well; d. separating the micelle emulsion from any free water therein; e. heating the separated micelle emulsion at a temperature and time period sufficient to substantially break the micelle emulsion and produce a water layer free of paraffin and a hydrocarbon layer containing the paraffin dissolved therein; and f. separating the water from the hydrocarbon layer from step (e).
Claim 11
Independent Claim
267 words
A method for the recovery of paraffin solidified in producing oil wells in the form of usable hydrocarbon comprising the steps of: a. preparing a mixture of a paraffin-dispersing effective amount of an alkyl or aralkyl polyoxyalkylene phosphate ester surfactant in the free acid form, or in the form of the alkali metal, amine, or ammonium salt; a mutual solvent composed of a blend of an alcohol selected from the group consisting of aliphatic alcohols, glycols, polyglycols and glycol esters and mixtures thereof and an aromatic hydrocarbon selected from the group consisting of benzene, toluene, and xylene, and water, and heating said mixture to a temperature of from about 30° to 40° F. higher than the melting point of the paraffin to be removed to form a micelle, wherein the micelle mixture contains from about 8 to 35 weight percent of the phosphate ester surfactant, from about 65 to 95 weight percent of the mutual solvent, and from about 70 to 90 weight percent of water; b. contacting said micelle mixture with the interior of the oil well for a period of time sufficient to disperse paraffin within the well into the mixture; and c. removing the mixture and the paraffin dispersed therein from the interior of the well; d. separating the micelle emulsion from any free water therein; e. heating the separated micelle emulsion at a temperature and time period sufficient to substantially break the micelle emulsion and produce a water layer free of paraffin and a hydrocarbon layer containing the paraffin dissolved therein; and f. separating the water from the hydrocarbon layer from step (e).
Claim 12
Dependent Claim
58 words
The method of claim 9 wherein the phosphate ester surfactant and mutual solvent are first mixed together and then the water component at a temperature in the range from about 30° to 40° F. greater than the melting point of the paraffin to be removed is added to the first formed mixture to form the final heated mixture.
Claim 13
Dependent Claim
23 words
The method of claim 9 or 10 wherein the micelle emulsion is heated at a temperature of from about 120° to 180° F.
Claim 14
Dependent Claim
24 words
The method of claim 9 or 10 wherein the micelle emulsion is heated for a time period of from about 2 to 24 hours.
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