Process for oil recovery using surfactant gels

a technology of surfactant gel and oil recovery, which is applied in the field of crude oil recovery composition, can solve the problems of costly hydration unit for the polymer, serious formation damage, and the inability to widely use the eor process in the industry, and achieve the effect of increasing the viscosity of injection brin

Inactive Publication Date: 2007-06-21
BELGER PAUL DANIEL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0016] U.S. Pat. No. 4,825,950 uses a betaine as an IFT lowering surfactant along with two different polymers to form an electrolyte tolerant injection fluid for oil recovery. The first polymer is primarily for thickening and the second is used to prevent the first polymer and the surfactant from interfering with each other through interaction and / or precipitation.
[0018] The present invention requires minimum up-front investment and equipment for injection. In most cases, the produced water can be used as the injection water without any costly water treatment, softening and sludge disposal. It also minimizes any potential damage to the formation that may be caused by the incompatibility of the injected chemicals with the formation. BRIEF DESCRIPTION OF THE INVENTION
[0021] This amphoteric surfactant(s) is chosen and designed to be used alone to simultaneously reduce the IFT between water and oil and to increase the viscosity of the injection brine, or it can be used in combination with certain other surfactants and / or polymers in an aqueous injection fluid composition to recover oil by (a) injecting an effective amount of said composition into a subterranean oil containing formation through one or more injection wells, and (b) displacing the fluid into the formation, and recovering the oil through one or more production wells.

Problems solved by technology

Many EOR techniques have been disclosed in the past yet the EOR process is not widely used by the industry for several reasons.
Also, a costly hydration unit is often required for the polymer in order to properly dissolve and develop its viscosity.
In addition, the polyacrylamide may precipitate and cause serious formation damage when contacting the connate water containing multivalent cations.
Most polymers are not stable at temperatures above 140° C. and are irreversibly degraded by shear.
The huge up-front investment and product limitations currently discourage the wide use of the EOR process.
None of these examples of the prior art disclose the use of amphoteric surfactants, preferably alkyl amido betaines, specifically chosen and designed to be used in aqueous injection fluids and especially in produced brine without any water treatment or water softening to provide both low IFT and mobility control for the recovery of residual oil by injection into one or more injection wells, displacing the fluid into the formation, and recovering the oil from one or more production wells.

Method used

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  • Process for oil recovery using surfactant gels
  • Process for oil recovery using surfactant gels
  • Process for oil recovery using surfactant gels

Examples

Experimental program
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example 1

[0037] This example illustrates the use of an amphoteric alkyl amido betaine surfactant derived from naturally occurring vegetable oils, to simultaneously lower the IFT of the brine / oil and increase the viscosity of the brine for an Asian oil field application.

[0038] The amphoteric surfactant, designated as B0503-1, was prepared by reacting 0.333 mole of soybean oil with 1.000 mole of dimethyl amino propyl amine (DMAPA). The resulting soya amidopropyldimethyl amine was further reacted with sodium chloroacetate in the presence of the proper amount of a 1:1 by weight mixture of water and butyl cellosolve to produce the soya amidopropyldimethyl betaine (sample no. B0503-1) with an active concentration of 50% by weight.

[0039] The brine from an Asian oil field, designated as Oil Field A, contained 32,000 ppm total dissolved solids, 1,850 ppm of the multivalent cations, and the crude oil had an API Gravity of 22. The bottom hole temperature was 60° C.

[0040] The IFT was measured using a...

example 2

[0042] This example illustrates that B0503-1 from example 1 does not provide low IFT in Oil Field B—a west Texas Oil Field. This problem was resolved by adding an anionic surfactant along with the B0503-1 to give acceptable IFT and viscosity values.

[0043] The brine from the Field B contained 13,500 ppm total dissolved solids, 620 ppm multivalent cations and the crude oil had an API Gravity of 18. The bottom hole temperature was 48° C. B0503-2 was prepared by adding 1 part by weight of the sodium salt of C1416 arylalkyl xylene sulfonic acid, designated XSA-1416 and prepared as described according to U.S. Pat. No. 6,043,391, to 10 parts by weight of B0503-1. As shown in Table 2, B0503-1 used alone did not provide low IFT and proper viscosity in the oil and brine from Oil Field B. However, by adding the anionic surfactant the IFT was lowered and the viscosity was increased.

TABLE 2IFT and Viscosity Properties for Oil Field BB0503-1, 0.5%B0503-2, 0.5%IFT, mN / m0.0940.0085Visc @ 12 RPM,...

example 3

[0044] This example illustrates the oil recovery obtained from columns packed with crushed core from Oil Field B.

[0045] Two separate but identical columns were prepared by adding 150 grams of the oil saturated crushed core from Oil Field B to glass chromatography columns 7 inches long and 1 inch in diameter. The oil saturated crushed core was prepared by mixing 16% by weight of the crude oil with 84% by weight of the crushed core. The columns were carefully prepared to eliminate air during packing. The Pore Volume (PV) of the columns was determined to be approximately 70% or 105 ml. This is the amount of liquid required for one displacement through the column. Each column contained 150 g×0.16=24 g oil. Injection field brine was passed through the bottom of each column and collected in fractions of approximately 0.5 PV (approximately 52.5 ml) each from the top. The brine was injected into the bottom of the columns until all the free oil was removed. Then an additional 3.5 PV of the ...

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Abstract

A composition and process for recovering oil by injecting an aqueous solution into a subterranean oil-bearing formation through one or more injection wells, displacing the solution into the formation, and recovering the oil from one or more production wells. This aqueous solution contains one or more amphoteric alkyl amido betaine surfactants that form a viscoelastic surfactant gels that can reduce the interfacial tension (IFT) and increase the viscosity of the injection fluid simultaneously in certain oils and brines. These viscoelastic gels are tolerant to electrolytes and multivalent cations. They are shear reversible and adsorbed little on the reservoir rock. The viscosity of the gels is reduced when they encountered certain hydrocarbons but remains high when contacting water or brine. This allows the fluid to preferentially penetrate the oil-bearing portions of the formation and resulting additional oil recovery. These amphoteric viscoelastic surfactant gels are particular suitable for use with reservoirs and brines characterized by medium to high temperatures, higher salinity, higher concentrations of divalent cations, and low formation porosities.

Description

CROSS REFERENCE TO RELATED APPLICATIONS [0001] This application is based on provisional application Ser. No. 60 / 557,346, filed on Mar. 29, 2004 and is a Divisional application of previously filed 11 / 081,232 filed Mar. 16, 2005.STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT [0002] Not Applicable DESCRIPTION OF ATTACHED APPENDIX [0003] Not Applicable [0004] 1. Field of the Invention [0005] This invention relates to the field of Enhanced Oil Recovery (EOR). More specifically, it relates to a composition and process containing viscoelastic surfactant gels that have both surfactant and gelling properties that simultaneously provides low water / oil interfacial tension (IFT) and increases the viscosity of the injection fluid used for residual oil recovery. [0006] 2. Background of the Invention [0007] Crude oil is generally recovered from an oil-bearing reservoir by three processes, designated primary, secondary and tertiary recovery. The latter is also known as Enhanced Oil...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C09K8/58
CPCC09K8/584Y10S507/936
Inventor BERGER, PAUL D.BERGER, CHRISTIE H.
Owner BELGER PAUL DANIEL
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