US2839466A - Flooding composition - Google Patents
Flooding composition Download PDFInfo
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- US2839466A US2839466A US498040A US49804055A US2839466A US 2839466 A US2839466 A US 2839466A US 498040 A US498040 A US 498040A US 49804055 A US49804055 A US 49804055A US 2839466 A US2839466 A US 2839466A
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- water
- flooding
- sulfonic acid
- oil
- carboxylic acid
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/584—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
Definitions
- This invention relates to the recovery of oil from subterranean oil sands and oil-bearing strata by secondary flooding operations after depletion of primary production. More particularly thi-sinvention relates to an improved flood water composition for flooding clay-containing petroleum formations.
- alkyl aromatic sulfonic acid having a molecular weight of at least about 400.
- a more preferred alkyl aromatic sulfonic acid is one that has a molecular weight of not less than about 440. Since such sulfonic acids have only a very limited solubility in water, improved results are obtained when a water soluble carboxylic acid is used in conjunction with the sulfonic acid.
- Suitablecarboxylic acids are those which do not form an insoluble saltwith the alkaline earth metals, such as calcium, barium, magnesium, etc.
- Preferred carboxylic acids are the aliphatic acids containing not more than 4 carbon atoms as follows: formic, acetic, propionic, and butyric acids.
- Other suitable carboxylic acids include lactic, maleic, gluconic, and salicylic acids.
- the carboxylic acid may vary from about 25 to 200 parts per million of the fresh water. A more preferred rangeis 50 to 100 parts per million.
- the amount of the carboxylic acid used is within the same range as the sulfonic acid. Obviously greater quantities of the sulfonic acid and also the carboxylic acid could be used; however, such excessive use imparts no beneficial eifect and does increase the cost.
- a preferred sulfonic acid is that produced by sulfonating the detergent alkylate sometimes called polydodecylbenzene which consists of monoalkyl benzenes and dialkyl benzenes in the approximate ratio of 2:3. Its typical physical properties are as follows:
- Suchsulfonic acids in addition to the polydodecylbenzene sulfonic acid described above include the mahogany sulfonic acids produced by sulfuric acid treatment of lube stock petroleum fractions and the sulfonic acids of the naphthenic and than about 10,000 parts per million of dissolved'solidsto which has been added from about 25 to about 200 parts per million of alkyl aromatic sulfonic acid and a watersoluble carboxylic acid in approximately the same'amount, namely, 25 to 200 parts per million.
- a :cross-sectional area of core, cm. AP pressure drop through core in atmospheres
- Example 1 A non-saline water was flowed through a clay-containing core sample having an air permeability of 262 md. for a period of 30 hours. The permeability of the core throughout the flow period remained at approximately 10 md., which is shown in Figure 1 as curve A wherein permeability versus liquid throughput is plotted.
- Example 2 The water-flooded core sample of Example 1 was then subjected to flow flooding with a composition consisting of the same non-saline water containing 50 p. p. in. each of polydodecylbenzene sulfonic acid and acetic acid.
- a composition consisting of the same non-saline water containing 50 p. p. in. each of polydodecylbenzene sulfonic acid and acetic acid.
- Example 3 T A core sample having an air permeability of 420 1nd. was flow-flooded with a non-saline Water composition containing 100 p. p. m. each of polydodecylbenzene sulfonic acid and acetic acid. The initial permeability was 210 md., dropped ofl momentarily to recover, and rose steadily thereafter to an apparent steady rate of about 250 md. as is illustrated in Figure 2.
- Example 4 A core sample very similar to that used in Example 4 was flooded with a composition consisting of the nonsaline water containing 50 p. p. m. sulfonic acid and 50 p. p. m. of acetic acid.
- the core was also flooded with non-saline water alone. Where a non-saline water was used alone, permeability dropped to about percent of the original permeability While the core water-flooded with the water containing the sulfonic acid and the acetic acid showed a permeability of about 100 percent of the original permeability.
- a flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated therein to 200 p. p. In. of an alkaryl sulfonic acid which has a molecular weight of not less than 400 and 25 to 200 p. p. m. of a water soluble carboxylic acid containing from 1 to 7 carbon atoms, characterized further in that the alkaline earth metal salt of said carboxylic acid is water soluble.
- a flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated 4 therein 50 to 100 p. p. m. of an alkaryl sulfonic acid which has a molecular weight of not less than 400 and 50 to 100 p. p. m. of a water soluble carboxylic acid containing from 1 to 7 carbon atoms, characterized further in that the alkaline earth metal salt of said carboxylic acid is water soluble.
- a flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated therein 25 to 200 p. p. m. of an alkaryl sulfonic acid produced by sulfonating a mixture of monoalkylbenzene and dialkylbenzenes in the approximate ratio of 2:3, characterized in that the mixture of said alkylbenzenes have the following physical properties:
- a flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising Water as the major component having incorporated therein 25 to 200 p. p. m. of an alkaryl sulfonic acid which has a molecular weight of not less than 400 and 25 to 200 p. p. m. of an aliphatic acid containing not more than 4 carbon atoms characterized further in thatthe alkaline earth metal salts of said acid are water soluble.
- a flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated therein 25 to 200 p. p. m. of an alkaryl sulfonic acid which has a molecular Weight of not less than .400 and 25 to 200 p. p. m. of acetic acid.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
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Description
E 5 2 BE 0mm 00m OWN com On- 09 On 4 Sheets-Shee l lll?llll Illll D'ARCY A. SHOCK ETAL FLOODING COMPOSITION June 17, 1958 Filed March 30. 1955 q wuuw "HIH 'd INVENTOR. D'Arcy A. Shock BY John D. Sudbury E 2 N8 3 z 8 2 m June 17, 1958 D' ARCY A. SHOCK ETAL 2,839,466
FLOODING COMPOSITION 1 Filed March 30. 1955 4 Sheets-Sheet 3 .2 a a; 2 m "6 o 3 o. i U
a: E o a O o 3 9 I I E1 0 In I U U I) a i 8 m 0 Li. N l J I 9 X n- -lI-'- 0 0 O O o O (J g 9 8 m o n 3 m N ,(mgqnauua ou 6g.1o 5Q plowe INVENTOR.
DArey A. Shock BY John D. Sudbury June 17, 1958 D'ARCY A. SHOCK ETAL 2,839,466
FLOODING- COMPOSITION Filed March so. 1955 4 Sheets-Sheet 4 D'Arcy A-.$hock John D. Sudbury BY FLOQDING COMPOSITION DArcy A. Shock and John D. Sudbury, Ponca City, Okla, assignors to Continental Oil Company, Ponca City, Okla, a corporation of Delaware Application March 30, 1955, Serial No. 498,040
5 Claims. ((1252-3355) This invention relates to the recovery of oil from subterranean oil sands and oil-bearing strata by secondary flooding operations after depletion of primary production. More particularly thi-sinvention relates to an improved flood water composition for flooding clay-containing petroleum formations.
It is well known that oil-producing formations containing clays, such as the bentonites, undergo a marked decrease in injection rates when flooded with fresh water; i. e., water containing up to about 10,000 parts per million total solids. Because of the presence of such clays in the oil-bearing formation, it becomes impossible to maintain adequate injection rates of fresh water for the production of oil therefrom. 7
We have found that efficient injection rates can be maintained by the use of flood water containing an alkyl aromatic sulfonic acid having a molecular weight of at least about 400. A more preferred alkyl aromatic sulfonic acid is one that has a molecular weight of not less than about 440. Since such sulfonic acids have only a very limited solubility in water, improved results are obtained when a water soluble carboxylic acid is used in conjunction with the sulfonic acid. Suitablecarboxylic acids are those which do not form an insoluble saltwith the alkaline earth metals, such as calcium, barium, magnesium, etc. Preferred carboxylic acids are the aliphatic acids containing not more than 4 carbon atoms as follows: formic, acetic, propionic, and butyric acids. Other suitable carboxylic acids include lactic, maleic, gluconic, and salicylic acids. In no case should the carboxylic acid contain more than about 7 carbon atoms, otherwise, it will be rather insoluble in water. As to the amount of the sulfonic acid used, that may vary from about 25 to 200 parts per million of the fresh water. A more preferred rangeis 50 to 100 parts per million. Generally the amount of the carboxylic acid used is within the same range as the sulfonic acid. Obviously greater quantities of the sulfonic acid and also the carboxylic acid could be used; however, such excessive use imparts no beneficial eifect and does increase the cost.
A preferred sulfonic acid is that produced by sulfonating the detergent alkylate sometimes called polydodecylbenzene which consists of monoalkyl benzenes and dialkyl benzenes in the approximate ratio of 2:3. Its typical physical properties are as follows:
Specific gravity at 38 C 0.8649
Refractive index at 23 C 1.4900
Patented June 17, 1958 Viscosity at: -10 C. centipoises 2800 20 n 280 40 d0 :78 so ..do. 1s Aniline point C :69 Pour point F '25 As pointed out above sulfonic acids having amolecular weight greater than 400 are suitable. Suchsulfonic acids in addition to the polydodecylbenzene sulfonic acid described above include the mahogany sulfonic acids produced by sulfuric acid treatment of lube stock petroleum fractions and the sulfonic acids of the naphthenic and than about 10,000 parts per million of dissolved'solidsto which has been added from about 25 to about 200 parts per million of alkyl aromatic sulfonic acid and a watersoluble carboxylic acid in approximately the same'amount, namely, 25 to 200 parts per million.
In order to disclose more-clearly the nature of the present invention and the advantages thereof, reference will hereinafter be made to certain specific embodiments which illustrate the flexibility of the hereinafter described process. It should be clearly understood, however, that this is done solely by way of example and not to be construed as a limitation upon the spirit and scope of the appended claims. i
Core samples measuring /1 of an inch in diameter and i from one to two inches in length were tested under floodwherein K =permeability in millidarcies u=viscosity of liquid, centipoises L=length .of core, cm. I
A :cross-sectional area of core, cm. AP=pressure drop through core in atmospheres Example 1 A non-saline water was flowed through a clay-containing core sample having an air permeability of 262 md. for a period of 30 hours. The permeability of the core throughout the flow period remained at approximately 10 md., which is shown in Figure 1 as curve A wherein permeability versus liquid throughput is plotted.
Example 2 The water-flooded core sample of Example 1 was then subjected to flow flooding with a composition consisting of the same non-saline water containing 50 p. p. in. each of polydodecylbenzene sulfonic acid and acetic acid. In
this case the permeability of the core to the liquid rose to about 28 md., dropped ofl for a short period, and then rose again to a constant value of about 28 md. The results are represented by curve B of Figure 1 wherein permeability versus liquid throughput is plotted.
4 Example 3 T A core sample having an air permeability of 420 1nd. was flow-flooded with a non-saline Water composition containing 100 p. p. m. each of polydodecylbenzene sulfonic acid and acetic acid. The initial permeability was 210 md., dropped ofl momentarily to recover, and rose steadily thereafter to an apparent steady rate of about 250 md. as is illustrated in Figure 2.
Example 4 Example 5 A core sample very similar to that used in Example 4 was flooded with a composition consisting of the nonsaline water containing 50 p. p. m. sulfonic acid and 50 p. p. m. of acetic acid. For comparison purposes the core was also flooded with non-saline water alone. Where a non-saline water was used alone, permeability dropped to about percent of the original permeability While the core water-flooded with the water containing the sulfonic acid and the acetic acid showed a permeability of about 100 percent of the original permeability. These results are graphically illustrated in Figure 4.
Similar experiments were made in accordance with Example 4 with the exception that the following acids were substituted for the acetic acid: formic, propionic, butyric, maleic, gluconic acids. The results using these acids were very similar to that obtained using acetic acid.
What is considered new and inventive is defined in the hereunto appended claims, it being understood, of course, that equivalents known to those skilled in the art are to be construed as within the scope and purview of the claims.
7 Accordingly, applicants claim:
1. A flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated therein to 200 p. p. In. of an alkaryl sulfonic acid which has a molecular weight of not less than 400 and 25 to 200 p. p. m. of a water soluble carboxylic acid containing from 1 to 7 carbon atoms, characterized further in that the alkaline earth metal salt of said carboxylic acid is water soluble.
2. A flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated 4 therein 50 to 100 p. p. m. of an alkaryl sulfonic acid which has a molecular weight of not less than 400 and 50 to 100 p. p. m. of a water soluble carboxylic acid containing from 1 to 7 carbon atoms, characterized further in that the alkaline earth metal salt of said carboxylic acid is water soluble.
3. A flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated therein 25 to 200 p. p. m. of an alkaryl sulfonic acid produced by sulfonating a mixture of monoalkylbenzene and dialkylbenzenes in the approximate ratio of 2:3, characterized in that the mixture of said alkylbenzenes have the following physical properties:
Specific gravity at 38 C 0.8649 Average molecular weight 365 Percent sulfonatable 88 A. S. T. M..Dl 58 Engler:
I. B. P F 647 5 F 682 50 F 715 90 F.. 760 ..F.. 775 F. B. P ..F 779 Refractive index at 23 C 1.4900 Viscosity at:
-10 C. centipoises 2800 20 .d0 280 40 do 78 80 do 18 Aniline point C 69 Four point F -25 and 25 to 200 p. p. m. of a water soluble carboxylic acid containing from 1 to 7 carbon atoms, characterized further in that the alkaline earth metal salt of said carboxylic acid is water soluble.
4. A flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising Water as the major component having incorporated therein 25 to 200 p. p. m. of an alkaryl sulfonic acid which has a molecular weight of not less than 400 and 25 to 200 p. p. m. of an aliphatic acid containing not more than 4 carbon atoms characterized further in thatthe alkaline earth metal salts of said acid are water soluble.
5. A flooding process for recovering oil from a subterranean oil-bearing formation which consists in flooding said formation with an aqueous composition comprising water as the major component having incorporated therein 25 to 200 p. p. m. of an alkaryl sulfonic acid which has a molecular Weight of not less than .400 and 25 to 200 p. p. m. of acetic acid.
References Cited in the file of this patent UNITED STATES PATENTS Production, American Petroleum Institute, on May 22, 1941, 7 pages.
Claims (1)
1. A FLOODING PROCESS FOR RECOVERING OIL FROM A SUBTERRANEAN OIL-BEARING FORMATION WHICH CONSISTS IN FLOODING SAID FORMATION WITH AN AQUEOUS COMPOSITION COMPRISING WATER AS THE MAJOR COMPONENT HAVING INCORPORATED THEREIN 25 TO 200 P. P. M. OF AN ALKARYL SULFONIC ACID WHICH HAS A MOLECULAR WEIGHT OF NOT LESS THAN 400 AND 25 TO 200 P. P. M. OF A WATER SOLUBLE CARBOXYLIC ACID CONTAINING FROM 1 TO 7 CARBON ATOMS, CHARACTERIZED FURTHER IN THAT THE ALKALINE EARTH METAL SALT OF SAID CARBOXYLIC ACID IS WATER SOLUBLE.
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US498040A US2839466A (en) | 1955-03-30 | 1955-03-30 | Flooding composition |
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US498040A US2839466A (en) | 1955-03-30 | 1955-03-30 | Flooding composition |
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Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2941597A (en) * | 1959-06-08 | 1960-06-21 | Pure Oil Co | Secondary recovery |
US2978026A (en) * | 1958-01-07 | 1961-04-04 | California Research Corp | Well wash fluid |
US3141501A (en) * | 1960-08-26 | 1964-07-21 | Pure Oil Co | Control of permeability during water flooding |
DE1232534B (en) * | 1963-06-20 | 1967-01-19 | Continental Oil Co | Method for flooding oil deposits |
US3302713A (en) * | 1965-07-06 | 1967-02-07 | Exxon Production Research Co | Surfactant-waterflooding process |
US3315744A (en) * | 1964-12-31 | 1967-04-25 | Mobil Oil Corp | Dual function aqueous solution flow in permeable earth formations |
US3315743A (en) * | 1964-12-08 | 1967-04-25 | Mobil Oil Corp | Aqueous solution flow in permeable earth formations |
US3335793A (en) * | 1964-11-30 | 1967-08-15 | Cities Service Oil Co | Method and composition for improving and maintaining the capacity of water injection wells |
US3360043A (en) * | 1965-12-22 | 1967-12-26 | Texaco Inc | Method of treating clay-containing formations with guanidine salt solution |
US3361313A (en) * | 1966-08-08 | 1968-01-02 | Continental Oil Co | Agent for increasing viscosity of water-containing compositions |
US3392782A (en) * | 1966-08-15 | 1968-07-16 | Continental Oil Co | In situ preparation of surface active agents in subterranean formations |
US3434542A (en) * | 1967-10-09 | 1969-03-25 | Mobil Oil Corp | Waterflood process employing surfactant and graded viscosity |
US3444931A (en) * | 1967-11-24 | 1969-05-20 | Texaco Inc | Method of treating clay-containing formations with guanidine salt solution |
US3468377A (en) * | 1967-10-09 | 1969-09-23 | Mobil Oil Corp | Waterflooding employing surfactant solution |
US3480080A (en) * | 1968-03-22 | 1969-11-25 | Mobil Oil Corp | Waterflooding with an aqueous,saline solution of a hydrocarbon sulfonate having an optimum degree of sulfonation |
US3799263A (en) * | 1971-07-15 | 1974-03-26 | Exxon Production Research Co | Enhancing the recovery of oil from subterranean formations |
US3871454A (en) * | 1970-12-21 | 1975-03-18 | William M Harrison | Water flood process in clay-bearing subsurface formations |
US4217958A (en) * | 1978-11-24 | 1980-08-19 | Texaco Inc. | Sacrificial agents for petroleum recovery processes |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2356205A (en) * | 1942-10-21 | 1944-08-22 | Petrolite Corp | Process for increasing productivity of subterranean oil-bearing strata |
-
1955
- 1955-03-30 US US498040A patent/US2839466A/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2356205A (en) * | 1942-10-21 | 1944-08-22 | Petrolite Corp | Process for increasing productivity of subterranean oil-bearing strata |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2978026A (en) * | 1958-01-07 | 1961-04-04 | California Research Corp | Well wash fluid |
US2941597A (en) * | 1959-06-08 | 1960-06-21 | Pure Oil Co | Secondary recovery |
US3141501A (en) * | 1960-08-26 | 1964-07-21 | Pure Oil Co | Control of permeability during water flooding |
DE1232534B (en) * | 1963-06-20 | 1967-01-19 | Continental Oil Co | Method for flooding oil deposits |
US3335793A (en) * | 1964-11-30 | 1967-08-15 | Cities Service Oil Co | Method and composition for improving and maintaining the capacity of water injection wells |
US3315743A (en) * | 1964-12-08 | 1967-04-25 | Mobil Oil Corp | Aqueous solution flow in permeable earth formations |
US3315744A (en) * | 1964-12-31 | 1967-04-25 | Mobil Oil Corp | Dual function aqueous solution flow in permeable earth formations |
US3302713A (en) * | 1965-07-06 | 1967-02-07 | Exxon Production Research Co | Surfactant-waterflooding process |
US3360043A (en) * | 1965-12-22 | 1967-12-26 | Texaco Inc | Method of treating clay-containing formations with guanidine salt solution |
US3361313A (en) * | 1966-08-08 | 1968-01-02 | Continental Oil Co | Agent for increasing viscosity of water-containing compositions |
US3392782A (en) * | 1966-08-15 | 1968-07-16 | Continental Oil Co | In situ preparation of surface active agents in subterranean formations |
US3434542A (en) * | 1967-10-09 | 1969-03-25 | Mobil Oil Corp | Waterflood process employing surfactant and graded viscosity |
US3468377A (en) * | 1967-10-09 | 1969-09-23 | Mobil Oil Corp | Waterflooding employing surfactant solution |
US3444931A (en) * | 1967-11-24 | 1969-05-20 | Texaco Inc | Method of treating clay-containing formations with guanidine salt solution |
US3480080A (en) * | 1968-03-22 | 1969-11-25 | Mobil Oil Corp | Waterflooding with an aqueous,saline solution of a hydrocarbon sulfonate having an optimum degree of sulfonation |
US3871454A (en) * | 1970-12-21 | 1975-03-18 | William M Harrison | Water flood process in clay-bearing subsurface formations |
US3799263A (en) * | 1971-07-15 | 1974-03-26 | Exxon Production Research Co | Enhancing the recovery of oil from subterranean formations |
US4217958A (en) * | 1978-11-24 | 1980-08-19 | Texaco Inc. | Sacrificial agents for petroleum recovery processes |
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