High efficiency Brayton cycles using LNG
First Claim
1. A closed-loop Brayton power conversion system, comprising:
- A. a heat source;
B. a power turbine;
C. a recuperator;
D. a suction cooler;
E. a compressor;
F. a superheater;
G. an insulated storage tank for storing cold, liquefied heat sink media;
H. a pump for pumping the liquefied heat sink media from the storage tank (G) to the suction cooler (D);
I. primary coolant loop piping means for conveying a primary stream of a heat transfer gas in the following closed-loop flow sequence;
from component A to B to C to D to E, back to C, and then back to A;
wherein the entire sequence is cyclically repeated;
J. side-stream piping means for conveying a fraction of the heat transfer gas in a side-stream that splits-off from the primary coolant loop piping means at a first T-junction located in-between power turbine (B) and recuperator (C); and
then flows through superheater (F); and
finally to a second T-junction located in-between recuperator (C) and suction cooler (D);
at which point the side-stream is recombined with the primary stream of heat transfer gas before entering suction cooler (D); and
K. heat sink piping means for conveying the cold, liquefied heat sink media from storage tank (G) to pump (H);
then to suction cooler (D) where the liquefied heat sink media is substantially vaporized;
then to superheater (F); and
finally to exit piping means for delivering the vaporized heat sink media to market.
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Accused Products
Abstract
A modified, closed-loop Brayton cycle power conversion system that uses liquefied natural gas as the cold heat sink media. When combined with a helium gas cooled nuclear reactor, achievable efficiency can approach 68–76% (as compared to 35% for conventional steam cycle power cooled by air or water). A superheater heat exchanger can be used to exchange heat from a side-stream of hot helium gas split-off from the primary helium coolant loop to post-heat vaporized natural gas exiting from low and high-pressure coolers. The superheater raises the exit temperature of the natural gas to close to room temperature, which makes the gas more attractive to sell on the open market. An additional benefit is significantly reduced costs of a LNG revaporization plant, since the nuclear reactor provides the heat for vaporization instead of burning a portion of the LNG to provide the heat.
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Citations
18 Claims
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1. A closed-loop Brayton power conversion system, comprising:
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A. a heat source; B. a power turbine; C. a recuperator; D. a suction cooler; E. a compressor; F. a superheater; G. an insulated storage tank for storing cold, liquefied heat sink media; H. a pump for pumping the liquefied heat sink media from the storage tank (G) to the suction cooler (D); I. primary coolant loop piping means for conveying a primary stream of a heat transfer gas in the following closed-loop flow sequence;
from component A to B to C to D to E, back to C, and then back to A;
wherein the entire sequence is cyclically repeated;J. side-stream piping means for conveying a fraction of the heat transfer gas in a side-stream that splits-off from the primary coolant loop piping means at a first T-junction located in-between power turbine (B) and recuperator (C); and
then flows through superheater (F); and
finally to a second T-junction located in-between recuperator (C) and suction cooler (D);
at which point the side-stream is recombined with the primary stream of heat transfer gas before entering suction cooler (D); andK. heat sink piping means for conveying the cold, liquefied heat sink media from storage tank (G) to pump (H);
then to suction cooler (D) where the liquefied heat sink media is substantially vaporized;
then to superheater (F); and
finally to exit piping means for delivering the vaporized heat sink media to market. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 17)
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12. A method for converting power using a modified closed-loop Brayton power conversion system, comprising:
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a) providing a heat source (A), a power turbine (B), a recuperator (C), a suction cooler (D), a compressor (E), a superheater (F), an insulated storage tank for storing cold liquefied heat sink media (G), a pump (H) for pumping the liquefied heat sink media from storage tank (G) to suction cooler (D), and associated piping means; b) providing a heat transfer gas and a liquefied heat sink media to the system; c) conveying a primary stream of the heat transfer gas through closed-loop primary coolant loop piping means from component A to B to C to D to E, back to C, and then back to A;
followed by cyclically repeating the entire sequence;d) conveying a side-stream of heat transfer gas, split-off from the primary stream of heat transfer gas, from a first T-junction located in-between power turbine (B) and recuperator (C);
then to superheater (F); and
finally to a second T-junction located in-between recuperator (C) and suction cooler (D), where the side-stream is recombined with the primary stream of heat transfer gas before entering suction cooler (D); ande) pumping the liquefied heat sink media from storage tank (G) to suction cooler (D), where the liquefied heat sink media is substantially vaporized;
then to superheater (F) where the vaporized gas is heated; and
finally to exit piping means for delivering the vaporized heat sink media to market. - View Dependent Claims (13, 14, 15, 16, 18)
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Specification