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US4603154A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for preparing dilute polymer solutions

Assignee: Marathon Oil Co
•
Filing: 1985-06-19
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Granted: 1986-07-29
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Expires: 2005-06-19
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Abstract

Abstract A method for preparing dilute aqueous polymer solutions, especially dilute aqueous partially hydrolyzed polyacrylamide solutions, for use in secondary and tertiary oil recovery processes. The method comprises producing a concentrated polymer solution in a polymerization reactor and diluting the resulting gel-like, relatively high concentration polymer solution to obtain a free-flowing, relatively low concentration polymer solution by means of a staged dilution process. In each stage, an aqueous diluent is combined with the polymer solution to produce a nonuniform mixture which is maintained in a vessel in a quiescent state until the mixture becomes uniform. The stages are repeated as many times as necessary until the free-flowing, relatively low concentration polymer solution is obtained.

Inventors

  • 👤 Wayne E. Luetzelschwab

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 04:59
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/02; C08J3/03; B; B01; B01J; B01J14/00; B01J19/00; B01J19/24; B01J19/245; C09; C09K; C09K8/00; C09K8/58; C09K8/588; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00087; B01J2219/00103; B01J2219/00164; B01J2219/00166; C08J2300/00; C08J2300/10

Claims Analysis

Total Claims: 32
Claim 1
Independent Claim 289 words
A process for preparing a uniform dilute aqueous polymer solution used in enhanced oil recovery from a subterranean oil-bearing formation comprising: forming a slug of a polymerization mixture comprising a polymerizable substance and a polymerization initiator; introducing the slug into a polymerization vessel having an inlet and an outlet; repeating the formation of additional slugs of the polymerization mixture and sequentially introducing each additional slug into the polymerization vessel to form a reaction gradient between the slugs such that substantially no mixing occurs between each slug; controlling the rate of continuous movement of each slug in the polymerization vessel from the inlet to the outlet so that each slug is essentially completely polymerized to a polymer slug at the outlet; successively and continuously removing each polymer slug from the outlet; forming a reaction mixture by continuously introducing into each polymer slug a modifying agent capable of reacting with the polymer; continuously introducing the reaction mixture into a reaction vessel having an inlet and an outlet; controlling the rate of continuous movement of the reaction mixture in the reaction vessel from the inlet to the outlet such that the reaction between the polymer and the modifying agent is essentially complete at the outlet, forming a concentrated product solution; continuously removing the concentrated product solution from the outlet of the reaction vessel; mixing the concentrated product solution with an aqueous diluent without substantially degrading the polymer to obtain a nonuniform mixture of the concentrated product solution and aqueous diluent; introducing the nonuniform mixture into a dilution vessel; and maintaining the nonuniform mixture in the dilution vessel for a time sufficient to convert the nonuniform mixture to a uniform dilute polymer solution having a lower polymer concentration than the concentrated product solution.
Claim 2
Dependent Claim 289 words
A process for preparing a uniform dilute aqueous polymer solution used in enhanced oil recovery from a subterranean oil-bearing formation comprising: forming a slug of a polymerization mixture comprising a polymerizable substance and a polymerization initiator; introducing the slug into a polymerization vessel having an inlet and an outlet; repeating the formation of additional slugs of the polymerization mixture and sequentially introducing each additional slug into the polymerization vessel to form a reaction gradient between the slugs such that substantially no mixing occurs between each slug; controlling the rate of continuous movement of each slug in the polymerization vessel from the inlet to the outlet so that each slug is essentially completely polymerized to a polymer slug at the outlet; successively and continuously removing each polymer slug from the outlet; forming a reaction mixture by continuously introducing into each polymer slug a modifying agent capable of reacting with the polymer; continuously introducing the reaction mixture into a reaction vessel having an inlet and an outlet; controlling the rate of continuous movement of the reaction mixture in the reaction vessel from the inlet to the outlet such that the reaction between the polymer and the modifying agent is essentially complete at the outlet, forming a concentrated product solution; continuously removing the concentrated product solution from the outlet of the reaction vessel; mixing the concentrated product solution with an aqueous diluent without substantially degrading the polymer to obtain a nonuniform mixture of the concentrated product solution and aqueous diluent; introducing the nonuniform mixture into a dilution vessel; and maintaining the nonuniform mixture in the dilution vessel for a time sufficient to convert the nonuniform mixture to a uniform dilute polymer solution having a lower polymer concentration than the concentrated product solution.
Claim 3
Dependent Claim 81 words
The process of claim 1 additionally comprising a dilution stage of: mixing the uniform dilute polymer solution and aqueous diluent without substantially degrading the polymer to obtain a second nonuniform mixture; introducing the second nonuniform mixture into a second dilution vessel; and maintaining the second nonuniform mixture in the second dilution vessel for a time sufficient to convert the second nonuniform mixture to a uniform second dilute polymer solution having a lower polymer concentration than the first uniform dilute polymer solution.
Claim 4
Dependent Claim 38 words
The process additionally comprising repeating the dilution stage of claim 2 one or more times to obtain a final uniform dilute polymer solution having a lower polymer concentration than the dilute polymer solution of the immediately preceding stage.
Claim 5
Dependent Claim 24 words
The process of claim 1 wherein the polymer concentration of the concentrated product solution is from about 3.0 to about 15.0 percent by weight.
Claim 6
Dependent Claim 24 words
The process of claim 1 wherein the polymer concentration of the dilute polymer solution is from about 2.0 to about 12.0 percent by weight.
Claim 7
Dependent Claim 24 words
The process of claim 2 wherein the concentration of the second dilute polymer solution is from about 1.4 to about 9.0 percent by weight.
Claim 8
Dependent Claim 30 words
The process of claim 3 wherein the final dilute polymer solution is sufficiently miscible in the aqueous diluent upon contact so as not to form a stable interface upon contact.
Claim 9
Dependent Claim 22 words
The process of claim 3 wherein the concentration of the final dilute polymer solution is less than about 4.0 percent by weight.
Claim 10
Dependent Claim 19 words
The process of claim 1 wherein the concentrated polymer solution and aqueous diluent are mixed in a static mixer.
Claim 11
Dependent Claim 27 words
The process of claim 2 wherein the second dilution vessel is used to transport the second nonuniform mixture to a location remote from the first dilution vessel.
Claim 12
Dependent Claim 13 words
The process of claim 1 wherein the aqueous diluent is a fresh water.
Claim 13
Dependent Claim 12 words
The process of claim 1 wherein the aqueous diluent is a brine.
Claim 14
Dependent Claim 23 words
The process of claim 1 wherein the concentrated product solution is dispersed as discrete lumps throughout the aqueous diluent in the nonuniform mixture.
Claim 15
Dependent Claim 98 words
A process for dilution of a concentrated polymer solution having a gel-like consistency to a dilute aqueous polymer solution having a lower concentration than the concentrated polymer solution comprising: mixing the concentrated polymer solution with an aqueous diluent without substantially degrading the polymer to obtain a nonuniform mixture of the concentrated polymer solution and aqueous diluent; introducing the nonuniform mixture into a dilution vessel; and maintaining the nonuniform mixture in the dilution vessel for a time sufficient to convert the nonuniform mixture to a uniform dilute polymer solution having a lower polymer concentration than the concentrated polymer solution.
Claim 16
Dependent Claim 98 words
A process for dilution of a concentrated polymer solution having a gel-like consistency to a dilute aqueous polymer solution having a lower concentration than the concentrated polymer solution comprising: mixing the concentrated polymer solution with an aqueous diluent without substantially degrading the polymer to obtain a nonuniform mixture of the concentrated polymer solution and aqueous diluent; introducing the nonuniform mixture into a dilution vessel; and maintaining the nonuniform mixture in the dilution vessel for a time sufficient to convert the nonuniform mixture to a uniform dilute polymer solution having a lower polymer concentration than the concentrated polymer solution.
Claim 17
Dependent Claim 82 words
The process of claim 14 additionally comprising a second dilution stage of: mixing the uniform dilute polymer solution and aqueous diluent without substantially degrading the polymer to obtain a second nonuniform mixture; introducing the second nonuniform mixture into a second dilution vessel; and maintaining the second nonuniform mixture in the second dilution vessel for a time sufficient to convert the second nonuniform mixture to a uniform second dilute polymer solution having a lower polymer concentration than the first uniform dilute polymer solution.
Claim 18
Dependent Claim 38 words
The process of claim 15 additionally comprising repeating the dilution stage one or more times to obtain a final uniform dilute polymer solution having a lower polymer concentration than the dilute polymer solution of the immediately preceding stage.
Claim 19
Dependent Claim 24 words
The process of claim 14 wherein the polymer concentration of the concentrated product solution is from about 3.0 to about 15.0 percent by weight.
Claim 20
Dependent Claim 24 words
The process of claim 14 wherein the polymer concentration of the dilute polymer solution is from about 2.0 to about 12.0 percent by weight.
Claim 21
Dependent Claim 24 words
The process of claim 15 wherein the concentration of the second dilute polymer solution is from about 1.4 to about 9.0 percent by weight.
Claim 22
Dependent Claim 30 words
The process of claim 16 wherein the final dilute polymer solution is sufficiently miscible in the aqueous diluent not to form a stable interface upon contact with the aqueous diluent.
Claim 23
Dependent Claim 22 words
The process of claim 16 wherein the concentration of the final dilute polymer solution is less than about 4.0 percent by weight.
Claim 24
Dependent Claim 19 words
The process of claim 14 wherein the concentrated polymer solution and aqueous diluent are mixed in a static mixer.
Claim 25
Dependent Claim 27 words
The process of claim 15 wherein the second dilution vessel is used to transport the second nonuniform mixture to a location remote from the first dilution vessel.
Claim 26
Dependent Claim 13 words
The process of claim 14 wherein the aqueous diluent is a fresh water.
Claim 27
Dependent Claim 12 words
The process of claim 14 wherein the aqueous diluent is a brine.
Claim 28
Dependent Claim 23 words
The process of claim 14 wherein the concentrated product solution is dispersed as discrete lumps throughout the aqueous diluent in the nonuniform mixture.
Claim 29
Dependent Claim 13 words
The process of claim 1 wherein the polymerizable substance is an acrylamide monomer.
Claim 30
Dependent Claim 22 words
The process of claim 1 wherein the polymerizable substance is an acrylamide monomer and the modifying agent is an alkali metal hydroxide.
Claim 31
Dependent Claim 14 words
The process of claim 28 wherein the concentrated product solution comprises partially hydrolyzed polyacrylamide.
Claim 32
Dependent Claim 14 words
The process of claim 14 wherein the concentrated product solution comprises partially hydrolyzed polyacrylamide.

References Cited (Backward Citations)

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US2125245A Cited
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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) 1989-07-28 1990-01-27 1990-07-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-07-28 1994-01-27 1994-07-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-07-28 1998-01-27 1998-07-29 $7700.00 Window Closed / Lapsed

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