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US4126182A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for decreasing resistance to flow of crude oil up from a well or through a pipeline

Assignee: Texaco Inc
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Filing: 1978-02-27
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Granted: 1978-11-21
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Expires: 1998-02-27
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Abstract

Abstract Methods and mechanisms are disclosed comprising means for mixing only water with crude oil at temperatures above 32° F. until the inversion point is crossed where a lower viscosity emulsion consisting of oil-in-water is formed for reducing resistance to flow of crude oil up from deep in a well to the surface, or through a pipeline. This oil-in-water emulsion consists of, by volume, 5 percent to 15 percent oil and 95 percent to 85 percent water.

Inventors

  • 👤 Joseph C. Allen
  • 👤 Sze-Foo Chien

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 17:56
CPC Classifications
E; E21; E21B; E21B43/00; F; F17; F17D; F17D1/00; F17D1/08; F17D1/16; Y; Y10; Y10T; Y10T137/00; Y10T137/0318; Y10T137/0391

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 129 words
A method for flowing crude oil at temperatures above 32° F. from the bottom of a well to the surface with decreased resistance to flow comprising, (a) mixing only water with the crude oil at temperatures above 32° F. in the bottom of the well until an emulsion consisting of water and oil passes the inversion point where the emulsion transforms from a water-in-oil emulsion to a lower viscosity oil-in-water emulsion that contains, by volume, about 5 percent to 9 percent oil and 95 percent to 91 percent water, and (b) flowing the oil-in-water emulsion to the surface for producing more crude oil with less energy from a well than for producing unemulsified crude oil from the well utilizing expensive chemicals which are prohibitive in costs, practicality, and safety.
Claim 2
Independent Claim 129 words
A method for flowing crude oil at temperatures above 32° F. from the bottom of a well to the surface with decreased resistance to flow comprising, (a) mixing only water with the crude oil at temperatures above 32° F. in the bottom of the well until an emulsion consisting of water and oil passes the inversion point where the emulsion transforms from a water-in-oil emulsion to a lower viscosity oil-in-water emulsion that contains, by volume, about 5 percent to 9 percent oil and 95 percent to 91 percent water, and (b) flowing the oil-in-water emulsion to the surface for producing more crude oil with less energy from a well than for producing unemulsified crude oil from the well utilizing expensive chemicals which are prohibitive in costs, practicality, and safety.
Claim 3
Dependent Claim 31 words
A method as recited in claim 1 wherein the first step comprises, (a) mixing the oil-in-water into an emulsion that contains, by volume, about 5 percent oil and 95 percent water.
Claim 4
Dependent Claim 29 words
A method as recited in claim 1 wherein, (a) the step of flowing the oil-in-water emulsion comprises pumping the emulsion from the bottom of the well to the surface.
Claim 5
Independent Claim 123 words
A method for transporting crude oil at temperatures above 32° F. through a pipeline with decreased resistance to flow comprising, (a) mixing only water with the crude oil until the emulsion consisting of water and oil passes through the inversion point where the emulsion changes from a water-in-oil emulsion to a lower viscosity oil-in-water emulsion at temperatures above 32° F. that contains, by volume, about 5 percent to 9 percent oil and 95 percent to 91 percent water, and (b) transporting the oil-in-water emulsion at temperatures about 32° F. through the pipeline for transporting more crude oil more economically and with less energy than for transporting unemulsified crude oil through the pipeline utilizing expensive chemicals which are prohibitive in cost, practicality, and safety.
Claim 6
Independent Claim 123 words
A method for transporting crude oil at temperatures above 32° F. through a pipeline with decreased resistance to flow comprising, (a) mixing only water with the crude oil until the emulsion consisting of water and oil passes through the inversion point where the emulsion changes from a water-in-oil emulsion to a lower viscosity oil-in-water emulsion at temperatures above 32° F. that contains, by volume, about 5 percent to 9 percent oil and 95 percent to 91 percent water, and (b) transporting the oil-in-water emulsion at temperatures about 32° F. through the pipeline for transporting more crude oil more economically and with less energy than for transporting unemulsified crude oil through the pipeline utilizing expensive chemicals which are prohibitive in cost, practicality, and safety.
Claim 7
Dependent Claim 31 words
A method as recited in claim 4 wherein the first step comprises, (a) mixing the oil-in-water into an emulsion that contains, by volume, about 5 percent oil and 95 percent water.
Claim 8
Dependent Claim 24 words
A method as recited in claim 4 wherein, (a) the step of transporting the emulsion is performed by pumping the emulsion through the pipeline.

References Cited (Backward Citations)

US1192438A Cited
US2981683A Cited
US3196947A Cited
US3519006A Cited
US3425429A 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) 1981-11-20 1982-05-22 1982-11-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-11-20 1986-05-22 1986-11-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-11-20 1990-05-22 1990-11-21 $7700.00 Window Closed / Lapsed

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