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US4242870A Expired / Lapsed US ⏱️ 0.0 years remaining

Power systems using heat from hot liquid

Assignee: GE Oil and Gas Operations LLC
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Filing: 1974-08-29
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Granted: 1981-01-06
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Expires: 1994-08-29
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Abstract

Abstract The present invention relates to power systems and more particularly to systems in which hot water from a natural well or spring is used to vaporize a working fluid which is then expanded to produce mechanical energy. Improved working fluids are used which comprise mixtures of several fluids so chosen and combined in such proportions that the hot water is used more efficiently with the mixtures than would be possible with their individual components.

Inventors

  • 👤 Judson S. Searingen
  • 👤 Sham Sunder

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 21:05
CPC Classifications
F; F01; F01K; F01K25/00; F01K25/06

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 217 words
In a process for converting thermal energy to mechanical energy wherein a working fluid is pre-heated and vaporized by being passed through a heating zone in countercurrent heat exchange relation with a heating fluid, said working fluid is expanded to produce mechanical energy, and said working fluid is cooled and condensed, the improvement comprising: using as said working fluid a mixture of ingredient fluids having moderately close but essentially different boiling points such that said working fluid vaporizes over a desired range of substantially continuously increasing vaporization temperatures, wherein for a substantial increase in enthalpy of said working fluid as it passes through said heating zone there is a substantial increase in temperature of said working fluid, and the differences in temperature between said working fluid and said heating fluid at each point in said heating zone are more nearly equal than would be the differences in temperature between any of said ingredient fluids and said heating fluid at each point in said heating zone were said ingredient fluids passed individually through said heating zone in counter-current heat exchange relation with said heating fluid; maintaining substantially constant the respective compositions of said working fluid and said heating fluid throughout said heating zone; and further maintaining said heating fluid in substantially a single phase throughout said heating zone.
Claim 2
Dependent Claim 217 words
In a process for converting thermal energy to mechanical energy wherein a working fluid is pre-heated and vaporized by being passed through a heating zone in countercurrent heat exchange relation with a heating fluid, said working fluid is expanded to produce mechanical energy, and said working fluid is cooled and condensed, the improvement comprising: using as said working fluid a mixture of ingredient fluids having moderately close but essentially different boiling points such that said working fluid vaporizes over a desired range of substantially continuously increasing vaporization temperatures, wherein for a substantial increase in enthalpy of said working fluid as it passes through said heating zone there is a substantial increase in temperature of said working fluid, and the differences in temperature between said working fluid and said heating fluid at each point in said heating zone are more nearly equal than would be the differences in temperature between any of said ingredient fluids and said heating fluid at each point in said heating zone were said ingredient fluids passed individually through said heating zone in counter-current heat exchange relation with said heating fluid; maintaining substantially constant the respective compositions of said working fluid and said heating fluid throughout said heating zone; and further maintaining said heating fluid in substantially a single phase throughout said heating zone.
Claim 3
Dependent Claim 71 words
The process of claim 1 wherein said working fluid is cooled and condensed by being passed through a cooling zone in heat exchange relation with a cooling fluid and wherein the lowest temperature in said range of vaporization temperatures is substantially higher than the initial temperature of said cooling fluid, and the highest temperature in said range of vaporization temperatures is slightly lower than the initial temperature of said heating fluid.
Claim 4
Dependent Claim 17 words
The process of claim 1 including the step of superheating said working fluid in said heating zone.
Claim 5
Dependent Claim 50 words
The process of claim 1 wherein the relation between temperature and enthalpy of said working fluid as it passes through said heating zone is more nearly linear than would be the relation between temperature and enthalpy of any of said ingredient fluids were they passed individually through said heating zone.
Claim 6
Dependent Claim 53 words
The process of claim 2 wherein the difference in temperature between said working fluid and said heating fluid at a point of highest temperatures in said heating zone is less than the difference in temperature between said working fluid and said heating fluid at a point of lowest temperatures in said heating zone.
Claim 7
Dependent Claim 11 words
The process of claim 1 wherein said ingredient fluids are hydrocarbons.
Claim 8
Dependent Claim 40 words
The process of claim 1 wherein said working fluid is cooled and condensed by being passed through a cooling zone in countercurrent heat exchange relation with a cooling fluid, said working fluid condensing over a desired range of decreasing temperatures.
Claim 9
Dependent Claim 63 words
The process of claim 7 wherein the differences in temperature between said working fluid and said cooling fluid at each point in said cooling zone are more nearly equal than would be the differences in temperature between any of said ingredient fluids and said cooling fluid at each point in said cooling zone were said ingredient fluids passed individually through said cooling zone.
Claim 10
Dependent Claim 45 words
The process of claim 2 wherein said lowest temperature in said range of vaporization temperatures falls between predetermined lower and upper limits, said limits defining a set of values for which the process yields a desired amount of power per unit mass of heating fluid.
Claim 11
Dependent Claim 76 words
The process of claim 9 wherein said ingredient fluids are hydrocarbons, wherein said initial temperature of the cooling fluid and said initial temperature of the heating fluid define respective lower and upper extremes of a temperature spread, and wherein said lower limit is higher than said lower extreme by a value equal to 0.22 of said spread and said upper limit is higher than said lower extreme by a value equal to 0.7 of said spread.
Claim 12
Dependent Claim 75 words
The process of claim 9 wherein said ingredient fluids are hydrocarbons, wherein said initial temperature of the cooling fluid and said initial temperature of the heating fluid define respective lower and upper extremes of a temperature spread, and said lower limit is higher than said lower extreme by a value equal to 0.4 of said spread and said upper limit is higher than said lower extreme by a value equal to 0.55 of said spread.
Claim 13
Dependent Claim 12 words
The process of claim 1 wherein said heating fluid is substantially aqueous.

References Cited (Backward Citations)

GB465802A Cited
US3516248A Cited
US3757516A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-01-06 1984-07-07 1985-01-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-01-06 1988-07-07 1989-01-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-01-06 1992-07-07 1993-01-06 $7700.00 Window Closed / Lapsed

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