Granted Patent B2

US 12,516,855 · App. 17/974,913 · Granted Jan 6, 2026

Inventor: Timothy J. Held (Akron, OH)

Assignee: Supercritical Storage Company, Inc.

F25B30/02F25B6/00F25B40/00F25B9/008F25B2309/005F25B2309/06F25B2309/061F25B2339/047F25B2400/054F25B2400/141

Abstract

Claims (53)

1 . A dual rail heat pump cycle, comprising:

a low-temperature heat source;

a two-stage high-temperature heat exchanger unit comprising a first stage heat exchanger and a second stage heat exchanger through which, in operation, heat from a working fluid circulated within is transferred to a thermal medium moving through the high-temperature heat exchanger unit; and

a working fluid circuit for circulating the working fluid within the dual rail heat pump cycle and through the high-temperature heat exchanger unit, the working fluid circuit including:

an expander;

a compressor;

a recuperator unit interposed between the expander and the compressor, the recuperator unit comprising a first recuperator and a second recuperator and having a high-pressure side defined by the compressor and a low pressure side defined by the expander; wherein:

the cooled high-pressure working fluid exiting the first stage heat exchanger is divided at a first point in the working fluid circuit into a first portion and a second portion, the first portion entering the second stage heat exchanger directly to heat the thermal medium and be further cooled, exiting as a further cooled high-pressure first portion of the working fluid, the second portion entering the second recuperator directly to be cooled, exiting as a cooled high-pressure second portion of the working fluid,

the further cooled high-pressure first portion directly exiting the second stage heat exchanger and the cooled high-pressure second portion directly exiting the second recuperator being recombined at a second point in the working fluid circuit as a recombined high-pressure working fluid, thereby creating a pair of parallel flow paths between the first and second points directly between the second stage heat exchanger and the second recuperator, and

the recombined high-pressure working fluid further cooled in the first recuperator, exiting as a further cooled recombined high-pressure working fluid flowing to the expander.

2 . The dual rail heat pump cycle of claim 1 , wherein the dual rail heat pump cycle is an extended dual rail heat pump cycle and wherein:

the two-stage heat exchanger unit includes an extended stage heat exchanger;

the recombined high-pressure working fluid is further divided at a third point in the working fluid circuit prior to the first recuperator into a second set of first and second portions, the first portion directly entering the extended stage heat exchanger and exiting as a cooler first portion, the second portion directly entering the first recuperator and exiting as a cooler second portion, each of the cooler first and second portions recombined at a fourth point in the working fluid circuit upstream of the expander, thereby creating a second pair of parallel flow paths between the third and fourth points directly between the extended stage heat exchanger and the first recuperator.

3 . The dual rail heat pump cycle of claim 1 , wherein the thermal medium flows through the heat exchanger.

4 . The dual rail heat pump cycle of claim 1 , wherein the dual rail heat pump cycle is an extended dual rail heat pump cycle further comprising:

a third stage in the high-temperature heat exchanger; and

a second pair of parallel flow paths between the recuperator and the high-temperature heat exchanger.

5 . The dual rail heat pump cycle of claim 1 , further comprising:

a generator driven by the expander; and

a motor driving the compressor.

6 . The dual rail heat pump cycle of claim 1 , wherein the compressor is selected from a group comprising a fully hermetic reciprocating compressor a scroll compressor a centrifugal compressor.

7 . The dual rail heat pump cycle of claim 1 , wherein the expander includes at least one expansion device.

8 . The dual rail heat pump cycle of claim 7 , wherein the expansion device comprises an adiabatic expansion valve or a fluid expander.

9 . The dual rail heat pump cycle of claim 1 , wherein the expander is an adiabatic expansion valve or a fluid expander.

10 . The dual rail heat pump cycle of claim 9 , wherein the fluid expander is selected from a group comprising a turbine, a reciprocating expander, a scroll expander.

11 . A dual rail heat pump cycle, comprising:

a low-temperature heat source; and

a working fluid circuit through which, in operation, a working fluid circulates, the working fluid circuit including:

a recuperator;

a compression device defining a high-pressure side of the recuperator;

an expansion device downstream from the high-pressure side of recuperator, upstream from the low-temperature heat source, and defining a low-pressure side of the recuperator;

a pair of high-temperature first stage and second stage heat exchangers through which the thermal medium flows; and

a pair of parallel flow paths directly between the recuperator and the high-temperature second stage heat exchanger on the high-pressure side of the recuperator; wherein

the working fluid exits the compression device as a high-pressure working fluid that directly flows into the high-temperature first stage heat exchanger to release heat to the thermal medium and be cooled,

the high-pressure working fluid, directly upon exiting the high-temperature first stage heat exchanger is divided at a first point in the working fluid circuit into first and second portions, the first portion directly flowing into the high-temperature second stage heat exchanger to release heat to the thermal medium and be further cooled, the second portion directly flowing into the recuperator to be further cooled, each of the cooler first and second portions directly exiting the respective high-temperature second stage heat exchanger and recuperator being recombined at a second point in the working fluid circuit as a subsequently cooled high-pressure working fluid, thereby realizing the pair of parallel flow paths directly between the high-temperature second stage heat exchanger and the recuperator.

12 . The dual rail heat pump cycle of claim 11 , wherein the dual rail heat pump cycle is an extended dual rail heat pump cycle further comprising:

a third high-temperature heat exchanger through which the thermal medium flows; and

a second pair of parallel flow paths between the third high-temperature heat exchanger and the recuperator.

13 . The dual rail heat pump cycle of claim 11 , further comprising:

a generator driven by the expansion device; and

a motor driving the compression device.

14 . The dual rail heat pump cycle of claim 11 , wherein the compression device comprises a compressor.

15 . The dual rail heat pump cycle of claim 11 , wherein the compression device is selected from a group comprising a fully hermetic reciprocating compressor a scroll compressor a centrifugal compressor.

16 . The dual rail heat pump cycle of claim 11 , wherein the expansion device is an adiabatic expansion valve or a fluid expander.

17 . The dual rail heat pump cycle of claim 16 , wherein the fluid expander is selected from a group comprising a turbine, a reciprocating expander, a scroll expander.

18 . A working fluid circuit of a dual rail heat pump cycle, the working fluid circuit adapted to circulate a working fluid therethrough and through a pair of first and second stage heat exchangers that are part of the dual rail heat pump cycle, where heat from the working fluid circulated within the pair of first and second heat exchangers is transferred to a thermal medium moving through the pair of first stage and second stage heat exchangers, the working fluid circuit comprising, at least:

a compressor, and

at least one recuperator, wherein

the working fluid exits the compressor as a high-pressure working fluid that directly flows into the first stage heat exchanger to release heat to the thermal medium and be cooled,

the high-pressure working fluid directly exiting the first stage heat exchanger is divided into first and second portions, the first portion directly flowing into the second stage heat exchanger to release heat to the thermal medium and be further cooled, the second portion directly flowing into the at least one recuperator to be further cooled, each of the cooler first and second portions directly exiting the respective second stage heat exchanger and at least one recuperator being recombined as a subsequently cooled high-pressure working fluid, thereby realizing a pair of parallel flow paths directly between the second stage heat exchanger and the at least one recuperator so as to facilitate matching of heat capacities of the working fluid on either side of the first stage and second stage heat exchangers.

19 . The working fluid circuit of claim 18 , wherein the at least one recuperator is embodied as a recuperator unit comprising a first recuperator in series with a second recuperator, the pair of parallel flow paths arranged directly between the second stage heat exchanger and the second recuperator.

20 . The working fluid circuit of claim 19 , further comprising an expander, wherein the recombined high-pressure working fluid enters the first recuperator, exiting as a further cooled recombined high-pressure working fluid flowing to the expander to complete the dual rail heat pump cycle.

21 . The working fluid circuit of claim 19 , wherein the second portion of the divided high-pressure working fluid that directly exited the first stage heat exchanger flows only through the second recuperator before being recombined with the first portion of the divided high-pressure working fluid that exits the second stage heat exchanger.

Assignments (1)

Continuity (1)

References Cited (400)