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US4031706A Expired / Lapsed US ⏱️ 0.0 years remaining

Superheating steam from light water nuclear reactors

Assignee: General Electric Co
•
Filing: 1975-12-18
•
Granted: 1977-06-28
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Expires: 1995-12-18
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Abstract

Abstract Heat from an exothermic chemical reaction(s) is employed to superheat and/or reheat steam generated by a light water nuclear reactor (LWR). The use of such a source of heat enables the selection of a temperature for the heating limited by thermodynamic considerations that eliminates equipment failures due to overheating the heater tubes.

Inventors

  • 👤 Himanshu B. Vakil
  • 👤 Dale H. Brown

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 04:07
CPC Classifications
F; F01; F01K; F01K3/00; F01K3/18; F01K3/188; F24; F24V; F24V30/00

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 121 words
In a process for heating the pressurized steam product stream produced by heat generated in a light water nuclear reactor wherein the steam product stream is brought into heat exchange relationship with a high temperature source in a heat exchange device and the temperature of the steam product stream is increased to at least about 650° F. after which the superheated steam so produced is used to operate a steam turbine-generator set, the improvement comprising using a combustion-less exothermic chemical reaction for the generation of heat utilized for the heating step, said exothermic chemical reaction having a maximum attainable temperature limited by thermodynamic considerations to a value below the design capability of any component of said heat exchange device exposed thereto.
Claim 2
Dependent Claim 121 words
In a process for heating the pressurized steam product stream produced by heat generated in a light water nuclear reactor wherein the steam product stream is brought into heat exchange relationship with a high temperature source in a heat exchange device and the temperature of the steam product stream is increased to at least about 650° F. after which the superheated steam so produced is used to operate a steam turbine-generator set, the improvement comprising using a combustion-less exothermic chemical reaction for the generation of heat utilized for the heating step, said exothermic chemical reaction having a maximum attainable temperature limited by thermodynamic considerations to a value below the design capability of any component of said heat exchange device exposed thereto.
Claim 3
Dependent Claim 12 words
The improvement recited in claim 1 wherein the chemical reaction is methanation.
Claim 4
Dependent Claim 25 words
The improvement recited in claim 2 wherein the temperature of the methanation reaction is in the range of from about 1100° to about 1400° F.
Claim 5
Dependent Claim 14 words
The improvement recited in claim 1 wherein the chemical reaction is an oxidation-reduction reaction.
Claim 6
Dependent Claim 12 words
The improvement recited in claim 1 wherein the chemical reaction is hydrogenation.
Claim 7
Dependent Claim 23 words
The improvement recited in claim 1 wherein the exothermic chemical reaction is conducted at the delivery end of a closed loop chemical system.
Claim 8
Dependent Claim 12 words
The improvement recited in claim 6 wherein the chemical reaction is methanation.
Claim 9
Dependent Claim 36 words
The improvement recited in claim 1 wherein the superheated steam is supplied to a high pressure steam turbine, reheated with heat from an additional exothermic chemical reaction and then supplied to a low pressure steam turbine.
Claim 10
Dependent Claim 29 words
The improvement in claim 8 wherein the initial chemical reaction is methanation and the cooled products of the initial reaction are then reacted to provide the additional chemical reaction.
Claim 11
Dependent Claim 22 words
The improvement recited in claim 1 wherein the superheated steam produced has a temperature in the range of from about 1000°-1100° F.

References Cited (Backward Citations)

US3242053A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-06-27 1980-12-27 1981-06-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-27 1984-12-27 1985-06-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-27 1988-12-27 1989-06-28 $7700.00 Window Closed / Lapsed

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