US20100083677A1 - Economized refrigerant system utilizing expander with intermediate pressure port - Google Patents
Economized refrigerant system utilizing expander with intermediate pressure port Download PDFInfo
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- US20100083677A1 US20100083677A1 US12/527,625 US52762507A US2010083677A1 US 20100083677 A1 US20100083677 A1 US 20100083677A1 US 52762507 A US52762507 A US 52762507A US 2010083677 A1 US2010083677 A1 US 2010083677A1
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- refrigerant
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- economizer
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- 239000003507 refrigerant Substances 0.000 title claims abstract description 126
- 238000000034 method Methods 0.000 claims abstract description 17
- 238000007906 compression Methods 0.000 claims description 13
- 230000006835 compression Effects 0.000 claims description 12
- 238000010079 rubber tapping Methods 0.000 claims 1
- 238000011084 recovery Methods 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 abstract description 3
- 230000003993 interaction Effects 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/06—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using expanders
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
Definitions
- This application relates to economized refrigerant systems utilizing an expander as an expansion device, where at least a portion of refrigerant is tapped from a location in the expander at which it has been at least partially expanded, and is used to subcool a main refrigerant flow during heat transfer interaction in an economizer heat exchanger.
- a single expander can provide both an expansion function for a main expansion device of the refrigerant system, and further, an expansion function for an auxiliary economizer circuit expansion device of the refrigerant system.
- Refrigerant systems are known, and circulate a refrigerant through a refrigerant cycle to condition a secondary fluid.
- a compressor compresses a refrigerant and delivers it to a first heat exchanger.
- Refrigerant from that first heat exchanger passes through an expansion process, at which its pressure is lowered. Downstream of the expansion process, a refrigerant passes through a secondary heat exchanger, and then back to the compressor.
- a refrigerant flow is tapped from a main refrigerant flow, typically downstream of the first heat exchanger. This tapped refrigerant is passed through an expansion device, and then the expanded tapped refrigerant passes in heat exchange relationship with a main refrigerant flow in an economizer heat exchanger. In this manner, the refrigerant in the main refrigerant flow line is sub-cooled such that it will have a greater heating capacity when it reaches the second heat exchanger. The tapped refrigerant is returned to an intermediate compression point downstream of the economizer heat exchanger.
- This invention relates to economized refrigerant systems, where a single expander is utilized for refrigerant expansion, and further, where this single expander has at least one intermediate expansion port and provides an expansion function as a main expansion device and as at least one economizer circuit expansion device.
- the simplest economized refrigerant system configuration with a single economizer circuit has an expander with only one intermediate expansion port. However, for example, if a refrigerant system incorporates more than one economizer circuits, the number of serially located intermediate expander ports can be increased accordingly.
- a corresponding refrigerant system compressor can consist of multiple serially connected stages or can be a single internally economized compressor (this, for example, is a common arrangement for scroll or screw compressors).
- An electrical or mechanical connection between the expander and any of the individual compressors or compression stages can be arranged accordingly to recover at least a portion of energy released during the refrigerant expansion process.
- the expander can also be used to assist in driving any other components within or outside of the refrigerant system.
- a portion of refrigerant partially expanded by the expander is tapped at the intermediate expansion point and passed through an economizer heat exchanger in heat exchange relationship with a main refrigerant flow to provide additional subcooling to the main refrigerant flow and consequently enhance system performance.
- a single intermediate pressure tap is formed in the expander to tap at least a portion of the refrigerant for passage through a single economizer heat exchanger.
- FIG. 1 shows a prior art refrigerant system.
- FIG. 2 shows a first schematic of an inventive refrigerant system.
- FIG. 3 shows a second schematic inventive refrigerant system.
- FIG. 1 An economized refrigerant system 20 , as known in the prior art, is illustrated in FIG. 1 .
- two compressors 22 and 24 arranged serially may operate to provide two sequential stages of compression.
- a compressed refrigerant passes through a condenser 26 , and eventually through a main expansion device 28 .
- the expansion device 28 is illustrated as a valve, as mentioned above, it is also known to use an expander instead of the valve 28 . In the latter case, at least a portion of energy could be recovered during the refrigerant expansion process in the expander, for the main portion of the refrigerant passing to the evaporator 30 , where additional thermal potential is also provided to increase the cooling capacity of the refrigerant system 20 due to more efficient isentropic expansion process in the expander.
- Downstream of the main expansion device 28 the refrigerant passes through an evaporator 30 and then back to the compressor 22 .
- An economizer heat exchanger 32 is incorporated into the circuitry of the refrigerant system 20 .
- a tap line 34 taps a portion of the refrigerant from a main liquid line and passes that refrigerant through an economizer expansion device 36 .
- the partially expanded economizer circuit refrigerant is at a lower pressure and temperature, and thus cools the main refrigerant flow during heat transfer interaction in the economizer heat exchanger 32 .
- the tapped refrigerant is shown flowing in the same direction through the economizer heat exchanger 32 , it is typical to arrange the refrigerant flows in a counterflow configuration. However, for illustration simplicity, the two refrigerant streams are shown flowing in the same direction in this FIG. 1 .
- the tapped partially expanded portion of refrigerant is returned through a return line 38 to an intermediate compression point between the compression stages 22 and 24 . While a multi-stage compressor is illustrated in the FIG. 1 , and the economized refrigerant return line 38 is positioned between the two compression stages 22 and 24 , it is also known to return the economized portion of refrigerant to an intermediate point in a single compressor.
- FIG. 2 provides benefits from the inclusion of the economizer circuit. However, as a minimum it requires a second expansion device 36 . Also, if the expander is used to substitute the main expansion valve 28 , only a portion of the available expansion energy is recovered, since no energy recovery can be obtained from the economized portion of refrigerant passing through the tap line 34 and the economizer circuit expansion valve 36 .
- the present invention is shown in one example in FIG. 2 .
- the refrigerant system 40 in FIG. 2 also includes two sequential compressors 42 and 44 .
- a condenser 46 is positioned upstream of an economizer heat exchanger 48 , and an expander 50 .
- the expander 50 serves to expand a refrigerant and recover work of expansion, by electrical or mechanical means, as shown schematically at 54 .
- This recovered energy can be utilized to assist in driving of at least one of the components within or outside of the refrigerant system 40 .
- the expansion of the refrigerant through an expander 50 produces additional thermal potential for the fully expanded refrigerant entering an evaporator 56 and partially expanded refrigerant entering the heat exchanger 48 , due to a more efficient isentropic expansion process in the expander 50 , thus enhancing performance of the refrigerant system 40 .
- two compressors are shown in FIG. 2
- the present invention would also extend to refrigerant systems having a single compressor incorporating vapor injection or more than two sequential compression stages.
- a portion of the refrigerant is tapped from an intermediate pressure tap 51 in the expander 50 and passed through a line 52 and through the economizer heat exchanger 48 .
- the intermediate pressure tap point 51 is at a thermodynamic state at which the refrigerant has been at least partially expanded in the expander 50 .
- the refrigerant from the tap line 52 will subcool the refrigerant in the main liquid line passing through the economizer heat exchanger 48 during heat transfer interaction between these two refrigerant streams.
- Refrigerant is again returned through a line 53 to the mid-point between the stages 42 and 44 .
- the main portion of the refrigerant that is not tapped off through the intermediate pressure tap 51 continues to flow through the expander, undergoing further expansion, and thus adding to the expansion process work recovery and providing additional thermal potential to the refrigerant entering the evaporator 56 .
- an evaporator 56 is positioned downstream of the expander 50 , and the main portion of refrigerant passes through the evaporator 56 and to the compressor 42 .
- the expander 50 is as known in the art, except it has an additional intermediate pressure tap point 51 to supply a portion of the partially expanded refrigerant to the economizer heat exchanger 48 .
- the tap 51 may be an additional port in an expander housing that communicates with intermediate expansion point inside the expander.
- This embodiment achieves the inclusion of the economizer circuit without the need for a separate economizer expansion device (prior art element 36 ) and provides additional recovery of the expansion work benefiting the performance of the refrigerant system 40 .
- FIG. 3 shows yet another embodiment 140 .
- the expander 150 has two intermediate pressure tap points located serially with respect to the expansion process.
- a first economizer circuit and an economizer heat exchanger 142 is supplied with a portion of partially expanded refrigerant from a corresponding tap point 164 leading to a line 144 and a first return line 143 .
- This embodiment shows the return line 143 leading to a mid-point between the compression stages 42 and 44 .
- a second economizer heat exchanger 146 is supplied with a portion of further, but not fully, expanded refrigerant form a corresponding tap point 165 leading to a line 148 , and returned to a line 145 .
- FIG. 3 illustrates the return line 145 connecting to an intermediate compression point in the compressor 42 .
- the FIG. 3 embodiment is similar to the embodiment shown in FIG. 2 .
- the present invention thus provides at least partially expanded refrigerant for use in an economizer circuit without the need for a separate dedicated economizer expansion device and enhances capacity and efficiency of the refrigerant system.
- compressor and expander types could be used in this invention.
- scroll, screw, rotary or reciprocating compressors and expanders can be employed.
- the refrigerant systems that utilize this invention can be used in many different applications, including, but not limited to, air conditioning systems, heat pump systems, marine container units, refrigeration truck-trailer units, and supermarket refrigeration systems.
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- Physics & Mathematics (AREA)
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- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Other Air-Conditioning Systems (AREA)
Abstract
A refrigerant system utilizes an expander, where at least partially expanded refrigerant portion is tapped at the intermediate expansion point and passed through an economizer heat exchanger. In the economizer heat exchanger, the tapped refrigerant further cools refrigerant in a main liquid line. The present invention eliminates the need for a separate dedicated economizer circuit expansion throttling device, by utilizing a single expander to provide this expansion function. This invention also allows for the recovery of the expansion work, otherwise lost in the economizer expansion throttling device. System capacity and efficiency are improved by providing additional thermal potential for the refrigerant expanded (partially or fully) in the expander during more efficient isentropic process. In various embodiments, there may be more than a single economizer circuit, with each of said economizer circuits receiving the tapped refrigerant portions from the expander at different intermediate expansion points.
Description
- This application relates to economized refrigerant systems utilizing an expander as an expansion device, where at least a portion of refrigerant is tapped from a location in the expander at which it has been at least partially expanded, and is used to subcool a main refrigerant flow during heat transfer interaction in an economizer heat exchanger. In this manner, a single expander can provide both an expansion function for a main expansion device of the refrigerant system, and further, an expansion function for an auxiliary economizer circuit expansion device of the refrigerant system.
- Refrigerant systems are known, and circulate a refrigerant through a refrigerant cycle to condition a secondary fluid. Typically, a compressor compresses a refrigerant and delivers it to a first heat exchanger. Refrigerant from that first heat exchanger passes through an expansion process, at which its pressure is lowered. Downstream of the expansion process, a refrigerant passes through a secondary heat exchanger, and then back to the compressor.
- One additional option in a refrigerant system design is the use of an economizer function. In an economizer function, a refrigerant flow is tapped from a main refrigerant flow, typically downstream of the first heat exchanger. This tapped refrigerant is passed through an expansion device, and then the expanded tapped refrigerant passes in heat exchange relationship with a main refrigerant flow in an economizer heat exchanger. In this manner, the refrigerant in the main refrigerant flow line is sub-cooled such that it will have a greater heating capacity when it reaches the second heat exchanger. The tapped refrigerant is returned to an intermediate compression point downstream of the economizer heat exchanger.
- This invention relates to economized refrigerant systems, where a single expander is utilized for refrigerant expansion, and further, where this single expander has at least one intermediate expansion port and provides an expansion function as a main expansion device and as at least one economizer circuit expansion device. The simplest economized refrigerant system configuration with a single economizer circuit has an expander with only one intermediate expansion port. However, for example, if a refrigerant system incorporates more than one economizer circuits, the number of serially located intermediate expander ports can be increased accordingly. A corresponding refrigerant system compressor can consist of multiple serially connected stages or can be a single internally economized compressor (this, for example, is a common arrangement for scroll or screw compressors). An electrical or mechanical connection between the expander and any of the individual compressors or compression stages can be arranged accordingly to recover at least a portion of energy released during the refrigerant expansion process. The expander can also be used to assist in driving any other components within or outside of the refrigerant system. A portion of refrigerant partially expanded by the expander is tapped at the intermediate expansion point and passed through an economizer heat exchanger in heat exchange relationship with a main refrigerant flow to provide additional subcooling to the main refrigerant flow and consequently enhance system performance.
- In one embodiment, a single intermediate pressure tap is formed in the expander to tap at least a portion of the refrigerant for passage through a single economizer heat exchanger. In a second embodiment, there are two intermediate pressure taps and two economizer heat exchangers associated with these taps. Of course, a worker of ordinary skill in the art would recognize that even more taps and more corresponding economizer circuits can be formed and included into the refrigerant system design.
- These and other features of the present invention can be best understood from the following specification and drawings, the following of which is a brief description.
-
FIG. 1 shows a prior art refrigerant system. -
FIG. 2 shows a first schematic of an inventive refrigerant system. -
FIG. 3 shows a second schematic inventive refrigerant system. - An economized
refrigerant system 20, as known in the prior art, is illustrated inFIG. 1 . As shown, twocompressors - A compressed refrigerant passes through a
condenser 26, and eventually through amain expansion device 28. While theexpansion device 28 is illustrated as a valve, as mentioned above, it is also known to use an expander instead of thevalve 28. In the latter case, at least a portion of energy could be recovered during the refrigerant expansion process in the expander, for the main portion of the refrigerant passing to theevaporator 30, where additional thermal potential is also provided to increase the cooling capacity of therefrigerant system 20 due to more efficient isentropic expansion process in the expander. Downstream of themain expansion device 28, the refrigerant passes through anevaporator 30 and then back to thecompressor 22. Aneconomizer heat exchanger 32 is incorporated into the circuitry of therefrigerant system 20. As shown, atap line 34 taps a portion of the refrigerant from a main liquid line and passes that refrigerant through aneconomizer expansion device 36. The partially expanded economizer circuit refrigerant is at a lower pressure and temperature, and thus cools the main refrigerant flow during heat transfer interaction in theeconomizer heat exchanger 32. While the tapped refrigerant is shown flowing in the same direction through theeconomizer heat exchanger 32, it is typical to arrange the refrigerant flows in a counterflow configuration. However, for illustration simplicity, the two refrigerant streams are shown flowing in the same direction in thisFIG. 1 . The tapped partially expanded portion of refrigerant is returned through areturn line 38 to an intermediate compression point between thecompression stages FIG. 1 , and the economizedrefrigerant return line 38 is positioned between the twocompression stages - As mentioned above, the prior art shown in
FIG. 1 provides benefits from the inclusion of the economizer circuit. However, as a minimum it requires asecond expansion device 36. Also, if the expander is used to substitute themain expansion valve 28, only a portion of the available expansion energy is recovered, since no energy recovery can be obtained from the economized portion of refrigerant passing through thetap line 34 and the economizercircuit expansion valve 36. The present invention is shown in one example inFIG. 2 . Therefrigerant system 40 inFIG. 2 also includes twosequential compressors condenser 46 is positioned upstream of aneconomizer heat exchanger 48, and anexpander 50. As known, theexpander 50 serves to expand a refrigerant and recover work of expansion, by electrical or mechanical means, as shown schematically at 54. This recovered energy can be utilized to assist in driving of at least one of the components within or outside of therefrigerant system 40. Also, the expansion of the refrigerant through anexpander 50 produces additional thermal potential for the fully expanded refrigerant entering anevaporator 56 and partially expanded refrigerant entering theheat exchanger 48, due to a more efficient isentropic expansion process in theexpander 50, thus enhancing performance of therefrigerant system 40. Further, while two compressors are shown inFIG. 2 , the present invention would also extend to refrigerant systems having a single compressor incorporating vapor injection or more than two sequential compression stages. - A portion of the refrigerant is tapped from an
intermediate pressure tap 51 in theexpander 50 and passed through aline 52 and through theeconomizer heat exchanger 48. The intermediatepressure tap point 51 is at a thermodynamic state at which the refrigerant has been at least partially expanded in theexpander 50. The refrigerant from thetap line 52 will subcool the refrigerant in the main liquid line passing through theeconomizer heat exchanger 48 during heat transfer interaction between these two refrigerant streams. Refrigerant is again returned through a line 53 to the mid-point between thestages intermediate pressure tap 51 continues to flow through the expander, undergoing further expansion, and thus adding to the expansion process work recovery and providing additional thermal potential to the refrigerant entering theevaporator 56. As with theFIG. 1 refrigerant system 20, anevaporator 56 is positioned downstream of theexpander 50, and the main portion of refrigerant passes through theevaporator 56 and to thecompressor 42. Theexpander 50 is as known in the art, except it has an additional intermediatepressure tap point 51 to supply a portion of the partially expanded refrigerant to theeconomizer heat exchanger 48. Thetap 51 may be an additional port in an expander housing that communicates with intermediate expansion point inside the expander. A worker of ordinary skill in the art would recognize what is required to provide the disclosedexpander 50 and theintermediate pressure tap 51. - This embodiment achieves the inclusion of the economizer circuit without the need for a separate economizer expansion device (prior art element 36) and provides additional recovery of the expansion work benefiting the performance of the
refrigerant system 40. -
FIG. 3 shows yet anotherembodiment 140. In this embodiment, theexpander 150 has two intermediate pressure tap points located serially with respect to the expansion process. Here, a first economizer circuit and aneconomizer heat exchanger 142 is supplied with a portion of partially expanded refrigerant from acorresponding tap point 164 leading to aline 144 and afirst return line 143. This embodiment shows thereturn line 143 leading to a mid-point between the compression stages 42 and 44. A secondeconomizer heat exchanger 146 is supplied with a portion of further, but not fully, expanded refrigerant form acorresponding tap point 165 leading to aline 148, and returned to aline 145. - This embodiment illustrates the
return line 145 connecting to an intermediate compression point in thecompressor 42. In all other aspects, theFIG. 3 embodiment is similar to the embodiment shown inFIG. 2 . - Further, while only two circuits are shown in
FIG. 2 , additional economizer circuits and intermediate pressure corresponding tap ports in theexpander 50 can be provided. The present invention thus provides at least partially expanded refrigerant for use in an economizer circuit without the need for a separate dedicated economizer expansion device and enhances capacity and efficiency of the refrigerant system. - It should be pointed out that many different compressor and expander types could be used in this invention. For example, scroll, screw, rotary or reciprocating compressors and expanders can be employed.
- The refrigerant systems that utilize this invention can be used in many different applications, including, but not limited to, air conditioning systems, heat pump systems, marine container units, refrigeration truck-trailer units, and supermarket refrigeration systems.
- Furthermore, it has to be understood that although this invention can be applied to any economized refrigerant systems, the refrigerant systems employing CO2 as a refrigerant would particularly benefit from this invention, since these systems have inherit deficiencies and require additional means for the performance enhancement.
- Although a preferred embodiment of this invention has been disclosed, a worker of ordinary skill in this art would recognize that certain modifications would come within the scope of this invention. For that reason, the following claims should be studied to determine the true scope and content of this invention.
Claims (16)
1. A refrigerant system comprising:
a compressor, said compressor compressing refrigerant and delivering it downstream to a first heat exchanger, refrigerant passing from said first heat exchanger through at least one economizer heat exchanger and an expander, refrigerant expanding in said expander,
a second heat exchanger positioned downstream of said expander, and refrigerant passing from said expander through said second heat exchanger, and then back to said compressor; and
at least a portion of refrigerant being tapped from at least one location where it has been at least partially expanded in said expander, and passed through said economizer heat exchanger to cool refrigerant in a main refrigerant circuit, said tapped refrigerant portion then being returned to said compressor.
2. The refrigerant system as set forth in claim 1 , wherein said tapped refrigerant is returned to at least one intermediate compression point in said compressor.
3. The refrigerant system as set forth in claim 1 , wherein said compressor includes a first stage compressor and a second stage compressor.
4. The refrigerant system as set forth in claim 3 , wherein said returned refrigerant being returned to a point intermediate said first stage compressor and said second stage compressor.
5. The refrigerant system as set forth in claim 1 , wherein there is one said economizer heat exchanger, and at least a portion of at least partially expanded refrigerant being tapped from one location in said expander and passed through said one economizer heat exchanger.
6. The refrigerant system as set forth in claim 1 , wherein there are at least two of said economizer heat exchangers, and refrigerant being tapped from two locations in said expander and passed through said at least two economizer heat exchangers.
7. The refrigerant system as set forth in claim 6 , wherein said tapped refrigerant for said at least two economizer heat exchangers being tapped from at least two distinct locations in said expander.
8. The refrigerant system as set forth in claim 1 , wherein work of expansion is utilized to assist in driving at least one component within or outside of said refrigerant system.
9. A method of operating a refrigerant system comprising the steps of:
(a) providing a compressor, said compressor compressing refrigerant and delivering it downstream to a first heat exchanger, refrigerant passing from said first heat exchanger through at least one economizer heat exchanger, and an expander, refrigerant expanding in said expander;
(b) providing a second heat exchanger positioned downstream of said expander, and refrigerant passing from said expander through said second heat exchanger, and then back to said compressor; and
(c) tapping at least a portion of refrigerant from at least one location where it has been at least partially expanded in said expander, and passing it through said economizer heat exchanger to cool refrigerant in a main refrigerant circuit, said tapped refrigerant portion then being returned to said compressor.
10. The method as set forth in claim 9 , wherein said tapped refrigerant is returned to at least one intermediate compression point in said compressor.
11. The method as set forth in claim 9 , wherein said compressor includes a first stage compressor and a second stage compressor.
12. The method as set forth in claim 11 , wherein said returned refrigerant being returned to a point intermediate said first stage compressor and second stage compressor.
13. The method as set forth in claim 9 , wherein there is one said economizer heat exchanger, and at least a portion of at least partially expanded refrigerant being tapped from one location in said expander and passed through said one economizer heat exchanger.
14. The method as set forth in claim 9 , wherein there are at least two of said economizer heat exchangers, and refrigerant being tapped from two locations in said expander and passed through said at least two economizer heat exchangers.
15. The method as set forth in claim 14 , wherein said tapped refrigerant for said at least two economizer heat exchangers being tapped from at least two distinct locations in said expander.
16. The method as set forth in claim 8 , wherein work of expansion is utilized to assist in driving at least one component within or outside of said refrigerant system.
Applications Claiming Priority (1)
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PCT/US2007/062777 WO2008105868A2 (en) | 2007-02-26 | 2007-02-26 | Economized refrigerant system utilizing expander with intermediate pressure port |
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US20100083677A1 true US20100083677A1 (en) | 2010-04-08 |
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US12/527,625 Abandoned US20100083677A1 (en) | 2007-02-26 | 2007-02-26 | Economized refrigerant system utilizing expander with intermediate pressure port |
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US (1) | US20100083677A1 (en) |
CN (1) | CN101617182B (en) |
HK (1) | HK1140253A1 (en) |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4918942A (en) * | 1989-10-11 | 1990-04-24 | General Electric Company | Refrigeration system with dual evaporators and suction line heating |
US5095712A (en) * | 1991-05-03 | 1992-03-17 | Carrier Corporation | Economizer control with variable capacity |
US5722255A (en) * | 1996-12-04 | 1998-03-03 | Brasz; Joost J. | Liquid ring flash expander |
US6694750B1 (en) * | 2002-08-21 | 2004-02-24 | Carrier Corporation | Refrigeration system employing multiple economizer circuits |
US6928828B1 (en) * | 2004-01-22 | 2005-08-16 | Carrier Corporation | Tandem compressors with economized operation |
US7059151B2 (en) * | 2004-07-15 | 2006-06-13 | Carrier Corporation | Refrigerant systems with reheat and economizer |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2196238C2 (en) * | 2000-08-16 | 2003-01-10 | ТУЗОВА Алла Павловна | Method of recovery of natural gas expansion energy |
US6898941B2 (en) * | 2003-06-16 | 2005-05-31 | Carrier Corporation | Supercritical pressure regulation of vapor compression system by regulation of expansion machine flowrate |
CN1285863C (en) * | 2004-04-13 | 2006-11-22 | 中国科学院理化技术研究所 | Multi-pressure-level mixed working medium cryogenic throttling refrigeration system |
-
2007
- 2007-02-26 US US12/527,625 patent/US20100083677A1/en not_active Abandoned
- 2007-02-26 CN CN2007800517868A patent/CN101617182B/en not_active Expired - Fee Related
- 2007-02-26 WO PCT/US2007/062777 patent/WO2008105868A2/en active Application Filing
-
2010
- 2010-06-28 HK HK10106306.4A patent/HK1140253A1/en not_active IP Right Cessation
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4918942A (en) * | 1989-10-11 | 1990-04-24 | General Electric Company | Refrigeration system with dual evaporators and suction line heating |
US5095712A (en) * | 1991-05-03 | 1992-03-17 | Carrier Corporation | Economizer control with variable capacity |
US5722255A (en) * | 1996-12-04 | 1998-03-03 | Brasz; Joost J. | Liquid ring flash expander |
US6694750B1 (en) * | 2002-08-21 | 2004-02-24 | Carrier Corporation | Refrigeration system employing multiple economizer circuits |
US20040035122A1 (en) * | 2002-08-21 | 2004-02-26 | Alexander Lifson | Refrigeration system employing multiple economizer circuits |
US6928828B1 (en) * | 2004-01-22 | 2005-08-16 | Carrier Corporation | Tandem compressors with economized operation |
US7059151B2 (en) * | 2004-07-15 | 2006-06-13 | Carrier Corporation | Refrigerant systems with reheat and economizer |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100077777A1 (en) * | 2006-10-27 | 2010-04-01 | Carrier Corporation | Economized refrigeration cycle with expander |
US8528359B2 (en) * | 2006-10-27 | 2013-09-10 | Carrier Corporation | Economized refrigeration cycle with expander |
US20100058783A1 (en) * | 2006-12-26 | 2010-03-11 | Alexander Lifson | Injection of refrigerant in system with expander |
US8356489B2 (en) * | 2006-12-26 | 2013-01-22 | Carrier Corporation | Injection of refrigerant in system with expander |
US20120167606A1 (en) * | 2009-10-07 | 2012-07-05 | Mitsubishi Electric Corporation | Refrigeration cycle apparatus |
EP2602571A1 (en) * | 2011-12-06 | 2013-06-12 | Robert Bosch Gmbh | Reversible heat pump device and method for its operation |
US10473369B2 (en) | 2015-05-15 | 2019-11-12 | Carrier Corporation | Staged expansion system and method |
US11585608B2 (en) | 2018-02-05 | 2023-02-21 | Emerson Climate Technologies, Inc. | Climate-control system having thermal storage tank |
US11149971B2 (en) | 2018-02-23 | 2021-10-19 | Emerson Climate Technologies, Inc. | Climate-control system with thermal storage device |
US11346583B2 (en) * | 2018-06-27 | 2022-05-31 | Emerson Climate Technologies, Inc. | Climate-control system having vapor-injection compressors |
JP2023017009A (en) * | 2018-10-02 | 2023-02-02 | ダイキン工業株式会社 | refrigeration cycle equipment |
JP7473833B2 (en) | 2018-10-02 | 2024-04-24 | ダイキン工業株式会社 | Refrigeration Cycle Equipment |
US12007150B2 (en) | 2018-10-02 | 2024-06-11 | Daikin Industries, Ltd. | Refrigeration cycle device |
IT201900006560A1 (en) * | 2019-05-07 | 2019-08-07 | Giuseppe Verde | Reverse cycle steam compression thermal machine |
WO2024076711A1 (en) * | 2022-10-06 | 2024-04-11 | Johnson Controls Tyco IP Holdings LLP | Heating, ventilation, air conditioning, and/or refrigeration system with heating and cooling operations |
Also Published As
Publication number | Publication date |
---|---|
WO2008105868A3 (en) | 2008-11-20 |
CN101617182B (en) | 2012-01-04 |
WO2008105868A2 (en) | 2008-09-04 |
HK1140253A1 (en) | 2010-10-08 |
CN101617182A (en) | 2009-12-30 |
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