US4079785A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Oil recovery method using in situ-partitioning surfactant flood systems
Assignee: Phillips Petroleum Co
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Filing: 1977-03-18
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Granted: 1978-03-21
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Expires: 1997-03-18
Abstract
Abstract Samples of oil from a formation to be flooded are equilibrated with a series of surfactant systems comprising a petroleum sulfonate surfactant, a cosurfactant having limited solubility in water and brine. By using sulfonates having an equivalent weight within the range of 375 to 500 and using cosurfactants having a solubility in water varying from 0.5 to 20 grams per 100 grams of water, some of the mixtures will partition into two or more phases while others will not. Then a separate sulfonate-cosurfactant-brine system is made up corresponding to one of those which partitions and the system is injected into the reservoir where on contact with the oil it forms a multiphase bank.
Inventors
- 👤 James E. Hessert
- 👤 David F. Boneau
- 👤 Richard L. Clampitt
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 15:07
CPC Classifications
C; C09; C09K; C09K8/00; C09K8/58; Y; Y10; Y10S; Y10S507/00; Y10S507/935; Y10S507/936; Y10S507/937; Y10S507/938
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
336 words
A process for recovering oil from a subterranean oil-bearing reservoir comprising the steps of: (a) injecting into said reservoir through at least one injection well a surfactant system corresponding in composition to one which causes a separation into at least two phases upon mixing as follows: mixing samples of oil from said reservoir with a series of surfactant systems, each of said systems comprising: water; 3 to 12 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight within the range of 375 to 500; 250 to 100,000 parts per million by weight of an electrolyte based on the weight of said water; and 1-12 weight percent based on the weight of said water of a cosurfactant, which cosurfactant has a solubility in water within the range of 0.5 to 20 grams/100 grams of water and wherein either the equivalent weight of said sulfonate and/or the solubility of said cosurfactant and/or the concentration of said electrolyte is different in each of said systems making up said series; and wherein one of said two phases is an oil rich microemulsion containing at least 85 percent of said petroleum sulfonate; (b) contacting the thus injected surfactant system with said oil in said reservoir to form in situ a bank comprising (1) a phase of said reservoir oil containing a small amount of said cosurfactant, (2) a microemulsion phase comprising (a) oil from said reservoir and (b) water, surfactant and cosurfactant from said injected surfactant system, said surfactant being in substantially higher concentration in said microemulsion phase than in said injected surfactant system; and (3) a phase comprising a majority of said water from said injected surfactant system, a portion of said cosurfactant from said injected surfactant system and a minor portion of said surfactant from said injected surfactant system; (c) thereafter injecting a mobility buffer fluid behind said bank; and (d) thereafter injecting a drive fluid behind said mobility buffer thus forcing said oil on toward a recovery well.
Claim 2
Dependent Claim
336 words
A process for recovering oil from a subterranean oil-bearing reservoir comprising the steps of: (a) injecting into said reservoir through at least one injection well a surfactant system corresponding in composition to one which causes a separation into at least two phases upon mixing as follows: mixing samples of oil from said reservoir with a series of surfactant systems, each of said systems comprising: water; 3 to 12 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight within the range of 375 to 500; 250 to 100,000 parts per million by weight of an electrolyte based on the weight of said water; and 1-12 weight percent based on the weight of said water of a cosurfactant, which cosurfactant has a solubility in water within the range of 0.5 to 20 grams/100 grams of water and wherein either the equivalent weight of said sulfonate and/or the solubility of said cosurfactant and/or the concentration of said electrolyte is different in each of said systems making up said series; and wherein one of said two phases is an oil rich microemulsion containing at least 85 percent of said petroleum sulfonate; (b) contacting the thus injected surfactant system with said oil in said reservoir to form in situ a bank comprising (1) a phase of said reservoir oil containing a small amount of said cosurfactant, (2) a microemulsion phase comprising (a) oil from said reservoir and (b) water, surfactant and cosurfactant from said injected surfactant system, said surfactant being in substantially higher concentration in said microemulsion phase than in said injected surfactant system; and (3) a phase comprising a majority of said water from said injected surfactant system, a portion of said cosurfactant from said injected surfactant system and a minor portion of said surfactant from said injected surfactant system; (c) thereafter injecting a mobility buffer fluid behind said bank; and (d) thereafter injecting a drive fluid behind said mobility buffer thus forcing said oil on toward a recovery well.
Claim 3
Dependent Claim
16 words
A method according to claim 1 wherein said injected surfactant system is preceded by a preflush.
Claim 4
Dependent Claim
22 words
A method according to claim 1 wherein said buffer fluid is water containing 50 to 20,000 parts per million of a polyacrylamide.
Claim 5
Dependent Claim
12 words
A method according to claim 1 wherein said cosurfactant is isobutyl alcohol.
Claim 6
Dependent Claim
21 words
A method according to claim 1 wherein said sulfonate has an aqueous equivalent weight within the range of 407 to 417.
Claim 7
Dependent Claim
31 words
A method according to claim 1 wherein said electrolyte is primarily NaCl present in the concentration within the range of 2,000 to 50,000 ppm based on the weight of said water.
Claim 8
Dependent Claim
16 words
A method according to claim 1 wherein said injected surfactant system is essentially free of oil.
Claim 9
Dependent Claim
27 words
A method according to claim 1 wherein said cosurfactant has a solubility in water within the range of 2 to 10 grams per 100 grams of water.
Claim 10
Dependent Claim
162 words
A method according to claim 1 wherein said injected surfactant system is essentially free of oil and is preceded by a preflush, said buffer fluid is water containing 200 to 5,000 parts per million by weight of a polyacrylamide, said cosurfactant is isobutyl alcohol, and is present in an amount within the range of 2 to 10 weight percent based on the weight of said water, and said sulfonate is present in an amount within the range of 4 to 8 weight percent based on the weight of said water, and has an equivalent weight within the range of 407 to 417, and wherein said electrolyte is primarily NaCl and is present in a concentration within the range of 2,000 to 50,000 ppm based on the weight of said water, said water and said NaCl together being present in an amount within the range of 85 to 95 weight percent based on the total weight of said water, NaCl, sulfonate and cosurfactant.
Claim 11
Dependent Claim
12 words
A method according to claim 1 wherein said formation is oil wet.
Claim 12
Dependent Claim
12 words
A method according to claim 1 wherein said formation is water wet.
Claim 13
Dependent Claim
40 words
A method according to claim 1 wherein said oil is a mid-continent crude characterized substantially as follows: ______________________________________
Base type: Intermediate
Gravity, ° API at 60° F
39.1
Pour Test, ° F.
+20
Sulfur, % 0.15
Hydrogen Sulfide
Negative
______________________________________
Claim 14
Dependent Claim
49 words
A method according to claim 1 wherein said sulfonate has an average equivalent weight of less than about 435 and/or said cosurfactant has a solubility of more than 5 g/100 g of water and said electrolyte comprises NaCl in a concentration within the range of 10,000 to 50,000 ppm.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-03-20 | 1981-09-19 | 1982-03-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-03-20 | 1985-09-19 | 1986-03-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-03-20 | 1989-09-19 | 1990-03-21 | $7700.00 | Window Closed / Lapsed |