US4644073A
Expired / Lapsed
US
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Permeability contrast correction employing a sulfate-free propionate-sequestered chromium (III) solution
Assignee: Phillips Petroleum Co
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Filing: 1985-03-11
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Granted: 1987-02-17
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Expires: 2005-03-11
Abstract
Abstract A sulfate-free clear green solution of chromium(III) propionate is prepared by mixing aqueous propionic acid containing up to 55 weight percent propionic acid with a chromium(VI) oxidant, such as a dichromate or chromate, and a sulfur-containing reductant, such as a bisulfite, which on reacting yields two phases: a lower sulfate-containing phase for discard or recycle and an upper phase solution of sulfate-free clear green propionate-sequestered chromium(III), the latter phase being stabilized with additional acid. The upper phase solution is useful for crosslinking polymeric viscosifiers such as partially hydrolyzed acrylamide-based polymers and the like in permeability contrast corrections in enhanced oil recovery operations.
Inventors
- 👤 Naim A. Mumallah
- 👤 Tod K. Shioyama
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 09:37
CPC Classifications
C; C09; C09K; C09K8/00; C09K8/60; C09K8/84; C09K8/86; C09K8/88; C09K8/887; C07; C07C; C07C51/00; C07C51/41; C07C51/412; C08; C08L; C08L1/00; C08L1/08; C08L1/26; C08L1/28; C08L5/00; C09K8/50; C09K8/504; C09K8/506; C09K8/508; C09K8/512; C09K8/52; C09K8/528; C09K8/58; C09K8/588; Y; Y10; Y10S; Y10S507/00; Y10S507/903; Y10S507/935
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
180 words
A method of producing a two phase liquid system wherein one phase is a stabilized chromium(III) propionate solution and the other phase is a sulfate-containing solution which comprises the steps of: (a) admixing a propionic acid source selected from propionic acid and propionic anhydride with water thereby forming an aqueous solution of propionic acid containing about 9 to 55 weight percent propionic acid; (b) adding to said aqueous propionic acid a chromium(VI) source selected from the group consisting of chromium(VI) oxide and alkali metal and ammonium dichromates and chromates thereby forming a solution of said chromium(VI) source in said aqueous propionic acid employing a molar ratio of at least about 4:1 propionic acid:chromium; (c) adding to said solution of chromium(VI) source in aqueous propionic acid, an inorganic sulfur-based compound as reducing agent wherein the valence of the sulfur is less than six, employing sufficient reducing agent, time and temperature to effectively reduce chromium(VI) to chromium(III) and simultaneously oxidize the reducing agent to sulfate and (d) separating said two phase liquid system into a sulfate-containing phase and a chromium(III) propionate-containing phase.
Claim 2
Independent Claim
180 words
A method of producing a two phase liquid system wherein one phase is a stabilized chromium(III) propionate solution and the other phase is a sulfate-containing solution which comprises the steps of: (a) admixing a propionic acid source selected from propionic acid and propionic anhydride with water thereby forming an aqueous solution of propionic acid containing about 9 to 55 weight percent propionic acid; (b) adding to said aqueous propionic acid a chromium(VI) source selected from the group consisting of chromium(VI) oxide and alkali metal and ammonium dichromates and chromates thereby forming a solution of said chromium(VI) source in said aqueous propionic acid employing a molar ratio of at least about 4:1 propionic acid:chromium; (c) adding to said solution of chromium(VI) source in aqueous propionic acid, an inorganic sulfur-based compound as reducing agent wherein the valence of the sulfur is less than six, employing sufficient reducing agent, time and temperature to effectively reduce chromium(VI) to chromium(III) and simultaneously oxidize the reducing agent to sulfate and (d) separating said two phase liquid system into a sulfate-containing phase and a chromium(III) propionate-containing phase.
Claim 3
Dependent Claim
13 words
The process according to claim 1 wherein said chromium(VI) source is potassium dichromate.
Claim 4
Dependent Claim
16 words
The process according to claim 2 wherein said sulfur-based reducing agent is sodium sulfite or bisulfite.
Claim 5
Dependent Claim
15 words
The process according to claim 3 wherein said propionic acid propionate source is propionic acid.
Claim 6
Dependent Claim
31 words
The process according to claim 1 wherein subsequent to said step (d) an additional acid selected from hydrochloric acid, acetic acid and propionic acid is added to said chromium(III) propionate-containing phase.
Claim 7
Dependent Claim
12 words
The process of claim 5 wherein said additional acid is hydrochloric acid.
Claim 8
Dependent Claim
12 words
The process of claim 5 wherein said additional acid is acetic acid.
Claim 9
Dependent Claim
24 words
The process of claim 1 employing in said step (b) propionic acid in a molar ratio range of about 4:1 to 45:1 propionic acid:chromium.
Claim 10
Dependent Claim
63 words
The process of claim 1 employing in said step (b) propionic acid in a molar ratio of at least about 4:1 propionic acid:chromium and subsequent to step (d) an additional acid selected from the group consisting of hydrochloric acid and acetic acid is added to said chromium(III) propionate-containing phase to bring total acidity to at least about an 11:1 molar ratio of acid:chromium.
Claim 11
Dependent Claim
26 words
The process of claim 1 employing a reaction time of about 0.5 to 24 hours, and a reaction temperature of about 40° C. to 100° C.
Claim 12
Dependent Claim
211 words
The stabilized chromium(III) propionate solution prepared by the process which comprises the steps of: (a) admixing a propionic acid source selected from the group consisting of propionic acid and propionic anhydride with water thereby forming an aqueous propionic acid solution containing 9 to 55 weight percent propionic acid; (b) adding to said aqueous propionic acid a chromium(VI) source selected from the group consisting of chromium(VI) oxide and alkali metal and ammonium dichromates and chromates thereby forming a solution of said chromium(VI) source in said aqueous propionic acid employing a molar ratio of at least 4:1 propionic acid:chromium; (c) adding to said solution of chromium(VI) source in aqueous propionic acid, an inorganic sulfur-based compound as reducing agent selected from the group consisting of alkali metal and ammonium bisulfites, sulfites, pyrosulfites, hydrosulfites and dithionites employing sufficient reducing agent, time and temperature to effectively reduce chromium(VI) to chromium(III) and simultaneously oxidize said reducing agent to sulfate thereby forming a sulfate-containing phase and a chromium(III) propionate-containing phase, (d) separating said phases and (e) further adding additional acid to said chromium(III) propionate-containing phase to adjust total acidity to at least about an 11:1 molar ratio of acid:chromium wherein said additional acid is selected from the group consisting of hydrochloric acid, acetic acid, propionic acid and mixtures.
Claim 13
Dependent Claim
211 words
The stabilized chromium(III) propionate solution prepared by the process which comprises the steps of: (a) admixing a propionic acid source selected from the group consisting of propionic acid and propionic anhydride with water thereby forming an aqueous propionic acid solution containing 9 to 55 weight percent propionic acid; (b) adding to said aqueous propionic acid a chromium(VI) source selected from the group consisting of chromium(VI) oxide and alkali metal and ammonium dichromates and chromates thereby forming a solution of said chromium(VI) source in said aqueous propionic acid employing a molar ratio of at least 4:1 propionic acid:chromium; (c) adding to said solution of chromium(VI) source in aqueous propionic acid, an inorganic sulfur-based compound as reducing agent selected from the group consisting of alkali metal and ammonium bisulfites, sulfites, pyrosulfites, hydrosulfites and dithionites employing sufficient reducing agent, time and temperature to effectively reduce chromium(VI) to chromium(III) and simultaneously oxidize said reducing agent to sulfate thereby forming a sulfate-containing phase and a chromium(III) propionate-containing phase, (d) separating said phases and (e) further adding additional acid to said chromium(III) propionate-containing phase to adjust total acidity to at least about an 11:1 molar ratio of acid:chromium wherein said additional acid is selected from the group consisting of hydrochloric acid, acetic acid, propionic acid and mixtures.
Claim 14
Dependent Claim
15 words
The stabilized chromium(III) propionate solution of claim 11 wherein said chromium(VI) source is sodium dichromate.
Claim 15
Dependent Claim
17 words
The stabilized chromium(III) propionate solution of claim 12 wherein said reducing agent is sodium bisulfite or sulfite.
Claim 16
Dependent Claim
16 words
The stabilized chromium(III) propionate solution of claim 13 wherein said propionic acid source is propionic acid.
Claim 17
Dependent Claim
15 words
The stabilized chromium(III) propionate solution of claim 14 wherein said additional acid is hydrochloric acid.
Claim 18
Dependent Claim
15 words
The stabilized chromium(III) propionate solution of claim 14 wherein said additional acid is acetic acid.
Claim 19
Dependent Claim
15 words
The stabilized chromium(III) propionate solution of claim 14 wherein said additional acid is propionic acid.
Claim 20
Dependent Claim
27 words
The stabilized chromium(III) propionate solution of claim 11 employing in said step (b) propionic acid in a molar ratio range of about 4:1 to 45:1 propionic acid:chromium.
Claim 21
Dependent Claim
55 words
The stabilized chromium(III) propionate solution of claim 11 employing in said step (b) propionic acid in a molar ratio of at least about 4:1 propionic acid:chromium, and in step (c) a further acid, selected from hydrochloric acid and acetic acid, to bring the total acidity to at least about an 11:1 molar ratio of acid:chromium.
Claim 22
Dependent Claim
27 words
The process according to claim 11 employing a reaction time of about 0.5 to 24 hours and a reaction temperature of about 40° C. to 100° C.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1990-02-16 | 1990-08-18 | 1991-02-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-02-16 | 1994-08-18 | 1995-02-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-02-16 | 1998-08-18 | 1999-02-17 | $7700.00 | Window Closed / Lapsed |