Patent Application
20210364202
Embodiments of the present disclosure relate generally to chiller systems used in air conditioning systems, and more particularly to a purge system for removing contaminants from a refrigeration system.
Chiller systems such as those utilizing centrifugal compressors may include sections that operate below atmospheric pressure. As a result, leaks in the chiller system may draw air into the system, contaminating the refrigerant. This contamination degrades the performance of the chiller system. To address this problem, existing low pressure chillers include a purge unit to remove contamination. Existing purge units typically use a vapor compression cycle to separate contaminant gas from the refrigerant. Existing purge units are complicated and lose refrigerant in the process of removing contamination.
Disclosed is a refrigeration system including a vapor compression loop and a purge system in communication with the vapor compression loop. The purge system includes at least one separator including a sorbent material to separate contaminants from a refrigerant purge gas provided from the vapor compression loop when a driving force is applied to the sorbent material.
In addition to one or more of the features described above, or as an alternative, in further embodiments including a prime mover selectively coupled to the at least one separator to apply a driving force to the sorbent material.
In addition to one or more of the features described above, or as an alternative, in further embodiments the prime mover is a vacuum pump.
In addition to one or more of the features described above, or as an alternative, in further embodiments the at least one separator is arranged in fluid communication with the vapor compression loop.
In addition to one or more of the features described above, or as an alternative, in further embodiments the vapor compression loop includes a compressor, a heat rejection heat exchanger, an expansion device, and a heat absorption heat exchanger connected by a conduit.
In addition to one or more of the features described above, or as an alternative, in further embodiments refrigerant passing through the sorbent material is returned to the at least one of the heat rejection heat exchanger and the heat absorption heat exchanger.
In addition to one or more of the features described above, or as an alternative, in further embodiments the purge system further includes a purge gas collector in communication with the at least one separator and at least one of the heat rejection heat exchanger and the heat absorption heat exchanger.
In addition to one or more of the features described above, or as an alternative, in further embodiments the purge gas collector comprises purge gas therein, the purge gas including refrigerant gas and contaminants.
In addition to one or more of the features described above, or as an alternative, in further embodiments said at least one separator includes a first separator and a second separator arranged in parallel.
In addition to one or more of the features described above, or as an alternative, in further embodiments including a flow control valve arranged upstream from an inlet end of both the first separator and the second separator, the flow control valve being selectively controllable to direct a flow toward one of the first separator and the second separator.
In addition to one or more of the features described above, or as an alternative, in further embodiments including a first valve arranged downstream from an outlet end of the first separator, wherein the first valve is movable between a first position and a second position.
In addition to one or more of the features described above, or as an alternative, in further embodiments when the first valve is in the first position, the prime mover is connected to the first separator and the outlet end of the first separator is in fluid communication with the vapor compression loop.
In addition to one or more of the features described above, or as an alternative, in further embodiments when the first valve is in the second position, the first separator is at ambient pressure, and the sorbent material is regenerated.
In addition to one or more of the features described above, or as an alternative, in further embodiments including a controller operably coupled to the flow control valve and to the prime mover.
In addition to one or more of the features described above, or as an alternative, in further embodiments the controller is operable to transform the flow control valve between a first position and a second position in response to a purge signal.
In addition to one or more of the features described above, or as an alternative, in further embodiments the purge signal is generated in response to an elapse of a predetermined amount of time.
In addition to one or more of the features described above, or as an alternative, in further embodiments the purge signal is generated in response to a measured parameter of the vapor compression system.
In addition to one or more of the features described above, or as an alternative, in further embodiments the sorbent material of the at least one separator is arranged in a bed.
In addition to one or more of the features described above, or as an alternative, in further embodiments the sorbent material of the at least one separator is arranged in a plurality of beds.
In addition to one or more of the features described above, or as an alternative, in further embodiments including a heat source in thermal communication with the sorbent material of the at least one separator.
In addition to one or more of the features described above, or as an alternative, in further embodiments the heat source is operable to generate the driving force applied to the sorbent material.
According to another embodiment, a method of operating a refrigeration system includes circulating a refrigerant through a vapor compression loop including a compressor, a heat rejecting heat exchanger, an expansion device, and a heat absorbing heat exchanger, collecting purge gas comprising contaminants from the vapor compression loop, and providing the purge gas to a separator pressurized by a prime mover to allow passage of refrigerant through a sorbent material and sorption of contaminants within the separator.
In addition to one or more of the features described above, or as an alternative, in further embodiments including collecting the purge gas in a purge gas collector positioned between the vapor compression loop and the separator.
In addition to one or more of the features described above, or as an alternative, in further embodiments including returning refrigerant that has passed through the sorbent material to the vapor compression loop.
In addition to one or more of the features described above, or as an alternative, in further embodiments including adjusting a pressure of the separator to regenerate the sorbent material.
The following descriptions should not be considered limiting in any way. With reference to the accompanying drawings, like elements are numbered alike:
A detailed description of one or more embodiments of the disclosed apparatus and method are presented herein by way of exemplification and not limitation with reference to the Figures.
Referring now to
The hot pressurized gaseous heat transfer fluid exiting from the compressor 12 flows through a conduit 20 to a heat rejection heat exchanger such as condenser 14. The condenser is operable to transfer heat from the heat transfer fluid to the surrounding environment, resulting in condensation of the hot gaseous heat transfer fluid to a pressurized moderate temperature liquid. The liquid heat transfer fluid exiting from the condenser 14 flows through conduit 22 to expansion valve 16, where the pressure is reduced. The reduced pressure liquid heat transfer fluid exiting the expansion valve 16 flows through conduit 24 to a heat absorption heat exchanger such as evaporator 18. The evaporator 18 functions to absorb heat from the surrounding environment and boil the heat transfer fluid. Gaseous heat transfer fluid exiting the evaporator 18 flows through conduit 26 to the compressor 12, so that the cycle may be repeated.
The vapor compression loop 10 has the effect of transferring heat from the environment surrounding the evaporator 18 to the environment surrounding the condenser 14. The thermodynamic properties of the heat transfer fluid must allow it to reach a high enough temperature when compressed so that it is greater than the environment surrounding the condenser 14, allowing heat to be transferred to the surrounding environment. The thermodynamic properties of the heat transfer fluid must also have a boiling point at its post-expansion pressure that allows the temperature surrounding the evaporator 18 to provide heat to vaporize the liquid heat transfer fluid.
Various types of refrigerant systems includes a vapor compression loop 10 as illustrated and described herein. One such refrigerant system is a chiller system. Portions of the refrigeration systems, such as the cooler of a chiller system for example, may operate at a low pressure (e.g., less than atmosphere) which can cause contamination (e.g., ambient air) to be drawn into the vapor compression loop 10 of the refrigeration system. The contamination degrades performance of the refrigeration system. To improve operation, the vapor compression loop 10 of a refrigeration system may additionally include a purge system 30 for removing contamination from the heat transfer fluid of the vapor compression loop 10.
With reference now to
The sorbent material 40 may be a porous inorganic material. Examples of suitable sorbent materials include, but are not limited to, zeolites, activated carbon, ionic liquids, metal organic framework, oils, clay materials, and molecular sieves for example. When the bed of sorbent material 40 is pressurized to a high, adsorption pressure, the more readily adsorbable component of the purge gas provided to the inlet end 42 of the separator 36 is selectively adsorbed by the sorbent material 40 and forms an adsorption front that passes from the inlet end 42 toward the outlet end 44. The less readily adsorbable component of the purge gas passes through the bed of sorbent material 40 and is recovered from the outlet end 44 thereof for further processing or use downstream. In the illustrated, non-limiting embodiment, the contaminant within the purge gas, such as oxygen for example, is the more readily adsorbable component, and the refrigerant is the less adsorbable component within the purge gas. Accordingly, if the purge gas is passed through a vessel 38 containing a bed of sorbent material 40 that attracts oxygen, part or all of the oxygen in the purge gas will stay within the bed of sorbent material 40. Consequently, the purge gas discharged from the outlet end 44 of the vessel 38 will be richer in refrigerant than the purge gas entering the vessel 38.
When the bed of sorbent material 40 reaches the end of its capacity to adsorb oxygen, the bed of sorbent material 40 can be regenerated by reducing the pressure acting thereon. By reducing the pressure, the adsorbed oxygen will be released from the bed of sorbent material 40, and may be exhausted from the separator 36, such as to the ambient atmosphere, external to the refrigeration circuit. However, it should be understood that in other embodiments, the bed of sorbent material may be regenerated via application of either a positive or negative pressure.
In some embodiments, pore sizes can be characterized by a pore size distribution with an average pore size from 2.5 Å to 10.0 Å, and a pore size distribution of at least 0.1 Å. In some embodiments, the average pore size for the porous material can be in a range with a lower end of 2.5 Å to 4.0 Å and an upper end of 2.6 Å to 10.0 Å. In some embodiments, the average pore size can be in a range having a lower end of 2.5 Å, 3.0 Å, 3.5 Å, and an upper end of 3.5 Å, 5.0 Å, or 6.0 Å. These range endpoints can be independently combined to form a number of different ranges, and all ranges for each possible combination of range endpoints are hereby disclosed. Porosity of the material can be in a range having a lower end of 5%, 10%, or 15%, and an upper end of 85%, 90%, or 95% (percentages by volume). These range endpoints can be independently combined to form a number of different ranges, and all ranges for each possible combination of range endpoints are hereby disclosed.
In some embodiments, the microporous material can be configured as nanoplatelets, such as zeolite nanosheets for example. Zeolite nanosheet particles can have thicknesses ranging from 2 to 50 nm, more specifically 2 to 20 nm, and even more specifically from 2 nm to 10 nm. Zeolite such as zeolite nanosheets can be formed from any of various zeolite structures, including but not limited to framework type MFI, MWW, FER, LTA, CHA, FAU, and mixtures of the preceding with each other or with other zeolite structures. In a more specific group of exemplary embodiments, the zeolite such as zeolite nanosheets can comprise zeolite structures selected from MFI, MWW, FER, LTA, CHA framework type. Zeolite nanosheets can be prepared using known techniques such as exfoliation of zeolite crystal structure precursors. For example, MFI and MWW zeolite nanosheets can be prepared by sonicating the layered precursors (multilamellar silicalite-1 and ITQ-1, respectively) in solvent. Prior to sonication, the zeolite layers can optionally be swollen, for example with a combination of base and surfactant, and/or melt-blending with polystyrene. The zeolite layered precursors are typically prepared using conventional techniques for preparation of microporous materials such as sol-gel methods.
A prime mover 50, such as a vacuum pump or compressor for example, may be selectively coupled to each of the plurality of separators 36. The prime mover 50 may be used to alter the pressure within the separators 36 and thereby control the sorption performed by the bed of sorbent material 40. Alternatively, or in addition, heat, such as generated by a heat source 51, may be used to control the sorption performed by the bed of sorbent material 40 (see
A valve 56 may similarly be arranged adjacent the outlet end 44 of each of the plurality of separators 36. The valve 56 is arranged at an interface between the outlet end 44 of the separator 36 and a conduit 58 for returning the refrigerant rich purge gas to the refrigerant fluid circulation loop, and specifically to the chiller or evaporator 18. In an embodiment, the valves 56 is operable to selectively connect the separator 36 to the prime mover 50 and the conduit 58.
A controller 60 is operably coupled to the prime mover 50 and the plurality of valves 52, 56 of the purge system 30. In an embodiment, the controller 60 receives system data (e.g., pressure, temperature, mass flow rates) and operates one or more components of the purge system 30 in response to the system data.
In an embodiment, the purge gas is provided to the plurality of separators 36 of the purge system 30 simultaneously. Alternatively, the purge gas may be provided to different separators 36 during different stages of operation, thereby allowing for continuous operation of the purge system 30. For example, with reference to
Once the bed of sorbent material 40 within the first separator 36A becomes saturated, the controller 60 will transform the purge system 30 to a second stage of operation by adjusting the position of upstream valve 52, and downstream valves 56. In an embodiment, the controller 60 is configured to transition between various stages of operation in response to a purge signal. The purge signal can be generated from various criteria. In some embodiments, the purge signal can be in response to elapse of a predetermined amount of time (e.g., simple passage of time, or tracked operating hours) tracked by controller circuitry. In some embodiments, the purge signal can be generated in response to human operator input. In some embodiments, the purge signal can be in response to measured parameters of the refrigerant fluid flow loop, such as a pressure sensor.
In the second stage of operation, best shown in
The term “about” is intended to include the degree of error associated with measurement of the particular quantity based upon the equipment available at the time of filing the application.
The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the present disclosure. As used herein, the singular forms “a”, “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “comprises” and/or “comprising,” when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, element components, and/or groups thereof.
While the present disclosure has been described with reference to an exemplary embodiment or embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the present disclosure. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the present disclosure without departing from the essential scope thereof. Therefore, it is intended that the present disclosure not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this present disclosure, but that the present disclosure will include all embodiments falling within the scope of the claims.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2019/063657 | 11/27/2019 | WO | 00 |
| Number | Date | Country | |
|---|---|---|---|
| 62774715 | Dec 2018 | US |
