WO2008105868A2 - Economized refrigerant system utilizing expander with intermediate pressure port - Google Patents
Economized refrigerant system utilizing expander with intermediate pressure port Download PDFInfo
- Publication number
- WO2008105868A2 WO2008105868A2 PCT/US2007/062777 US2007062777W WO2008105868A2 WO 2008105868 A2 WO2008105868 A2 WO 2008105868A2 US 2007062777 W US2007062777 W US 2007062777W WO 2008105868 A2 WO2008105868 A2 WO 2008105868A2
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- WIPO (PCT)
- Prior art keywords
- refrigerant
- expander
- heat exchanger
- tapped
- economizer
- Prior art date
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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.
- Figure 1 shows a prior art refrigerant system.
- Figure 2 shows a first schematic of an inventive refrigerant system.
- Figure 3 shows a second schematic inventive refrigerant system.
- FIG. 1 An economized refrigerant system 20, as known in the prior art, is illustrated in Figure 1. As shown, two compressors 22 and 24 arranged serially may operate to provide two sequential stages of compression. Alternatively, it is known to use a single compressor, where the refrigerant is injected at the intermediate compression point within the compression process. A compressed refrigerant passes through a condenser 26, and eventually through a main expansion device 28. While 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.
- 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. As shown, 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. While 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 Figure 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.
- the prior art shown in Figure 1 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 Figure 2.
- the refrigerant system 40 in Figure 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. Also, 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. Further, while two compressors are shown in Figure 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.
- Figure 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.
- This embodiment illustrates the return line 145 connecting to an intermediate compression point in the compressor 42.
- the Figure 3 embodiment is similar to the embodiment shown in Figure 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. Furthermore, it has to be understood that although this invention can be applied to any economized refrigerant systems, the refrigerant systems employing CO 2 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.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- 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
ECONOMIZED REFRIGERANT SYSTEM UTILIZING EXPANDER WITH INTERMEDIATE PRESSURE PORT
BACKGROUND OF THE INVENTION 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.
SUMMARY OF THE INVENTION 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.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 shows a prior art refrigerant system.
Figure 2 shows a first schematic of an inventive refrigerant system. Figure 3 shows a second schematic inventive refrigerant system.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An economized refrigerant system 20, as known in the prior art, is illustrated in Figure 1. As shown, two compressors 22 and 24 arranged serially may operate to provide two sequential stages of compression. Alternatively, it is known to use a single compressor, where the refrigerant is injected at the intermediate compression point within the compression process. A compressed refrigerant passes through a condenser 26, and eventually through a main expansion device 28. While 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. As shown, 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. While 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 Figure 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 Figure 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.
As mentioned above, the prior art shown in Figure 1 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 Figure 2. The refrigerant system 40 in Figure 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. As known, 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. Also, 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. Further, while two compressors are shown in Figure 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. As with the Figure 1 refrigerant system 20, 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. A worker of ordinary skill in the art would recognize what is required to provide the disclosed expander 50 and the intermediate 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.
Figure 3 shows yet another embodiment 140. In this embodiment, the expander 150 has two intermediate pressure tap points located serially with respect to the expansion process. Here, 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. This embodiment illustrates the return line 145 connecting to an intermediate compression point in the compressor 42. In all other aspects, the Figure 3 embodiment is similar to the embodiment shown in Figure 2.
Further, while only two circuits are shown in Figure 2, additional economizer circuits and intermediate pressure corresponding tap ports in the expander 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
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.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007800517868A CN101617182B (en) | 2007-02-26 | 2007-02-26 | Economized refrigerant system utilizing expander with intermediate pressure port |
| US12/527,625 US20100083677A1 (en) | 2007-02-26 | 2007-02-26 | Economized refrigerant system utilizing expander with intermediate pressure port |
| PCT/US2007/062777 WO2008105868A2 (en) | 2007-02-26 | 2007-02-26 | Economized refrigerant system utilizing expander with intermediate pressure port |
| HK10106306.4A HK1140253A1 (en) | 2007-02-26 | 2010-06-28 | Economized refrigerant system utilizing expander with intermediate pressure port |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US2007/062777 WO2008105868A2 (en) | 2007-02-26 | 2007-02-26 | Economized refrigerant system utilizing expander with intermediate pressure port |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2008105868A2 true WO2008105868A2 (en) | 2008-09-04 |
| WO2008105868A3 WO2008105868A3 (en) | 2008-11-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2007/062777 WO2008105868A2 (en) | 2007-02-26 | 2007-02-26 | Economized refrigerant system utilizing expander with intermediate pressure port |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20100083677A1 (en) |
| CN (1) | CN101617182B (en) |
| HK (1) | HK1140253A1 (en) |
| WO (1) | WO2008105868A2 (en) |
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| CN101568776B (en) * | 2006-10-27 | 2011-03-09 | 开利公司 | Economized refrigeration cycle with expander |
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| US11346583B2 (en) * | 2018-06-27 | 2022-05-31 | Emerson Climate Technologies, Inc. | Climate-control system having vapor-injection compressors |
| JP7193706B2 (en) | 2018-10-02 | 2022-12-21 | ダイキン工業株式会社 | refrigeration cycle equipment |
| CN109869940A (en) * | 2019-03-26 | 2019-06-11 | 天津商业大学 | Injecting type critical-cross carbon dioxide double-stage compressive refrigerating system |
| IT201900006560A1 (en) * | 2019-05-07 | 2019-08-07 | Giuseppe Verde | Reverse cycle steam compression thermal machine |
| CN112629089A (en) * | 2020-12-24 | 2021-04-09 | 珠海格力电器股份有限公司 | Control method of heat pump system, storage medium and heat pump system |
| 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 |
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| 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 |
| 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 |
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| US5722255A (en) * | 1996-12-04 | 1998-03-03 | Brasz; Joost J. | Liquid ring flash expander |
| 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 | Multiple pressure grade mixed working medium cryogenic throttling refrigeration system |
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2007
- 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
- 2007-02-26 US US12/527,625 patent/US20100083677A1/en not_active Abandoned
-
2010
- 2010-06-28 HK HK10106306.4A patent/HK1140253A1/en not_active IP Right Cessation
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| 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 |
| 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 |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100242532A1 (en) * | 2009-03-24 | 2010-09-30 | Johnson Controls Technology Company | Free cooling refrigeration system |
| US11175076B2 (en) | 2009-03-24 | 2021-11-16 | Johnson Controls Technology Company | Free cooling refrigeration system |
| US11199356B2 (en) | 2009-08-14 | 2021-12-14 | Johnson Controls Technology Company | Free cooling refrigeration system |
| EP2325577A3 (en) * | 2009-11-18 | 2014-05-21 | LG ELectronics INC. | Heat pump |
| EP2325578A3 (en) * | 2009-11-18 | 2014-05-21 | LG ELectronics INC. | Heat pump |
| US8789382B2 (en) | 2009-11-18 | 2014-07-29 | Lg Electronics Inc. | Heat pump including at least two refrigerant injection flow paths into a scroll compressor |
| WO2012040864A1 (en) | 2010-09-29 | 2012-04-05 | Erik Vincent Granwehr | Heat pump |
| EP3019364B1 (en) | 2013-07-08 | 2019-10-23 | Valeo Systèmes Thermiques | Temperature control system for a motor vehicle, corresponding heating, ventilation and/or air-conditioning equipment, and corresponding control method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101617182A (en) | 2009-12-30 |
| HK1140253A1 (en) | 2010-10-08 |
| CN101617182B (en) | 2012-01-04 |
| WO2008105868A3 (en) | 2008-11-20 |
| US20100083677A1 (en) | 2010-04-08 |
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