The present disclosure relates to a cascade refrigeration system having an upper portion that uses a modular chiller unit having ammonia as a refrigerant to provide condenser cooling for a refrigerant in a low temperature subsystem (for cooling low temperature loads) and/or for chilling a liquid that is circulated through a medium temperature subsystem (for cooling medium temperature loads). The present disclosure relates more particularly to a cascade refrigeration system having a critically-charged modular chiller unit that uses a sufficiently small charge of ammonia to minimize potential toxicity and flammability hazards. The present disclosure also relates more particularly to a modular ammonia cascade refrigeration system that uses a soluble or non-soluble oil with a particular oil control system mixed with the ammonia refrigerant charge. The present disclosure relates more particularly still to a modular ammonia cascade refrigeration system that uses an oil siphon arrangement to ensure positive return of oil from an evaporator of the modular ammonia chiller unit.
This section is intended to provide a background or context to the invention recited in the claims. The description herein may include concepts that could be pursued, but are not necessarily ones that have been previously conceived or pursued. Therefore, unless otherwise indicated herein, what is described in this section is not prior art to the description and claims in this application and is not admitted to be prior art by inclusion in this section.
Refrigeration systems typically include a refrigerant that circulates through a series of components in a closed system to maintain a cold region (e.g., a region with a temperature below the temperature of the surroundings). One exemplary refrigeration system includes a direct-expansion vapor-compression refrigeration system including a compressor. Such a refrigeration system may be used, for example, to maintain a desired low temperature within a low temperature controlled storage device, such as a refrigerated display case, coolers, freezers, etc. in a low temperature subsystem of the refrigeration system. Another exemplary refrigeration system includes a chilled liquid coolant circulated by a pump to maintain a desired medium temperature within a medium temperature storage device in a medium temperature subsystem of the refrigeration system. The low and/or medium temperature subsystems may each receive cooling from one or more chiller units in a cascade arrangement. The chiller units circulate a refrigerant through a closed-loop refrigeration cycle that includes an evaporator which provides cooling to the low temperature subsystem (e.g. as a condenser) and/or the medium temperature subsystem (e.g. as a chiller).
Accordingly, it would be desirable to provide a cascade refrigeration system having one or more modular chiller units capable of using ammonia as a refrigerant for providing condenser cooling in a low temperature subsystem of the refrigeration system, and/or for chilling a liquid coolant for circulation through a medium temperature subsystem of the refrigeration system.
One embodiment of the present disclosure relates to a cascade refrigeration system that includes an upper portion having at least one modular chiller unit that provides cooling to at least one low temperature subsystem having a plurality of low temperature loads, and a medium temperature subsystem having a plurality of medium temperature loads. The modular chiller unit includes a refrigerant circuit having at least a compressor, a condenser, an expansion device, and an evaporator. The modular chiller unit also includes an ammonia refrigerant configured for circulation within the refrigerant circuit, an ammonia refrigerant accumulator configured to receive the ammonia refrigerant from the evaporator, an oil recycling circuit having an oil separator, an oil filter, and oil pressure regulator, and an oil float, and an oil return line configured to reduce oil collection in the evaporator and to remove any collected oil from the evaporator. The modular chiller unit may also include an oil collection vessel (“oil pot”, etc.) that uses warmed coolant (e.g. glycol, etc.) to heat the oil being returned from the evaporator in order to boil-off entrained ammonia refrigerant prior to returning the oil to the ammonia refrigerant accumulator.
Another embodiment of the present disclosure relates to a modular ammonia chiller unit for a refrigeration system, including a refrigerant circuit having at least a compressor, a condenser, an expansion device, an evaporator, an ammonia refrigerant, an oil recycling circuit having an oil separator, an oil filter, an oil pressure regulator, and an oil reservoir, and an oil return line.
Yet another embodiment of the present disclosure relates to a cascade refrigeration system. A cascade refrigeration system includes an upper portion. The upper portion includes at least one modular chiller unit that provides cooling to at least one of a low temperature subsystem having a plurality of low temperature loads, and a medium temperature subsystem having a plurality of medium temperature loads. The modular chiller unit includes a refrigerant circuit, an ammonia refrigerant, an ammonia refrigerant accumulator, and an oil separation system. The refrigerant circuit includes at least a compressor, a condenser, an expansion device, and an evaporator. The ammonia refrigerant is configured for circulation within the refrigerant circuit. The ammonia refrigerant accumulator is configured to receive the ammonia refrigerant from the evaporator. The oil separation system is configured to remove oil from the ammonia refrigerant. The oil separation system includes an oil separator that is configured to remove oil from the ammonia refrigerant flowing from the compressor to the condenser, an oil drain pot that is configured to collect oil from the evaporator, and an oil reservoir that is configured to collect oil from the oil separator and the oil drain pot.
Yet another embodiment of the present disclosure relates to a method for supplying oil to a compressor in a modular chiller unit. The method includes the steps of receiving, at an ejector, a first amount of oil from an oil separator, wherein the first amount of oil is separated from ammonia that is passed through the oil separator; receiving, at an oil drain pot, an oil-ammonia mixture from an evaporator; heating liquid coolant by passing the liquid coolant over heads of the compressor, resulting in heated liquid coolant; heating the oil-ammonia mixture in the oil drain pot using the heated liquid coolant; determining an amount of liquid ammonia in the oil drain pot; receiving at the ejector, a second amount of oil from the oil drain pot; receiving, at an oil reservoir, a third amount of oil from the ejector, wherein the third amount of oil is a sum of the first amount of oil and the second amount of oil; and supplying a fourth amount of oil from the oil reservoir to the compressor.
Yet another embodiment of the present disclosure relates to an oil separation system for a modular chiller unit. The oil separation system includes an oil drain pot, an oil separator, an oil ejector, and an oil reservoir. The oil drain pot is configured to receive a first oil-ammonia mixture from an evaporator of the modular chiller unit. The oil separator is configured to collect oil from a second oil-ammonia mixture flowing from a compressor to a condenser in the modular chiller unit. The oil ejector is fluidically coupled to the oil drain pot and the oil separator. The oil ejector is configured to receive a first amount of oil from the oil drain pot and a second amount of oil from the oil separator. The oil reservoir is configured to receive a third amount of oil from the oil ejector. The third amount of oil is equal to a sum of the first amount of oil and the second amount of oil.
The disclosure will become more fully understood from the following detailed description, taken in conjunction with the accompanying figures, wherein like reference numerals refer to like elements, in which:
Referring to
The terms “low temperature” and “medium temperature” are used herein for convenience to differentiate between two subsystems of refrigeration system 10. Medium temperature subsystem 80 maintains one or more loads, such as cases 82 (e.g. refrigerator cases or other cooled areas) at a temperature lower than the ambient temperature but higher than low temperature cases 62. Low temperature subsystem 60 maintains one or more loads, such as cases 62 (e.g. freezer display cases or other cooled areas) at a temperature lower than the medium temperature cases. According to one exemplary embodiment, medium temperature cases 82 may be maintained at a temperature of approximately 20° F. and low temperature cases 62 may be maintained at a temperature of approximately minus (−) 20° F. Although only two subsystems are shown in the exemplary embodiments described herein, according to other exemplary embodiments, refrigeration system 10 may include more subsystems that may be selectively cooled in a cascade arrangement or other cooling arrangement.
An upper portion (e.g., the upper cascade portion 12) of the refrigeration system 10 includes one or more (shown by way of example as four) modular ammonia chiller units 20, that receive cooling from a cooling loop 14 having a pump 15, and one or more heat exchangers 16, such as an outdoor fluid cooler or outdoor cooling tower for dissipating heat to the exterior or outside environment. Outdoor fluid cooler 16 cools a coolant (e.g., water, etc.) that is circulated by pump 15 through cooling loop 17 to remove heat from the modular ammonia chiller units 20.
The ammonia chiller unit 20 is shown in more detail in
According to one alternative embodiment, the heat exchanger 26 (condenser) in the modular ammonia chiller unit 20 may be an air-cooled heat exchanger. For example, the air-cooled heat exchanger may be a microchannel type heat exchanger. According to another alternative embodiment, the air-cooled microchannel condenser may further include an evaporative component (such as water spray/baffles, etc.) to further enhance heat transfer of the air-cooled microchannel condenser. According to another embodiment, heat exchanger 16 in the water circulation loop 17 may be (or otherwise include) any of a wide variety of heat reclamation devices, such as may be associated with a facility where system 10 is installed. According to an exemplary embodiment, the term ‘critically charged’ is understood to mean a minimally sufficient amount of ammonia refrigerant necessary to accomplish the intended heat removal capacity for the chiller unit, without an excess amount of refrigerant (such as might be accommodated in a receiver of a non-critically charged system or device).
Referring further to
Referring further to
Referring to
Referring further to
Notably, in order to provide a chiller unit 20 that is less complex, less expensive, and more easily operated, serviced and maintained by technicians that may otherwise be unfamiliar with ammonia refrigerant systems, in exemplary embodiments, the chiller unit 20 may not include oil management components (e.g. piping, valves, controls, oil reservoir, filters, coolers, separators, float-switches, etc.) for providing lubrication to the compressor 24. For instance, in the illustrated embodiment of
Referring further to
According to one embodiment, the compressor 24 is a reciprocating, open-drive, direct-drive type compressor. According to other embodiments, other compressor types may be used, and/or additional components may be included, such as sight glasses, vent valves, and instrumentation such as pressure, flow and/or temperature sensors and switches, etc. In the embodiments of
According to one exemplary embodiment, the modular ammonia chiller units 20 are compact modular chiller units that are critically charged with a suitable amount of ammonia refrigerant, such as (by way of example) approximately 6-10 pounds of ammonia, or more particularly, approximately 8 pounds of ammonia. System 10 may include a multitude of the compact modular ammonia chiller units 20 arranged in parallel as low temperature refrigerant condensing units and/or as medium temperature liquid chillers. The number of compact modular ammonia chiller units 20 may be varied to accommodate various cooling loads associated with a particular commercial refrigeration system. Likewise, the number of medium temperature cases 82 and low temperature cases 62 may be varied.
Referring to
In order to provide further improved performance of the compact modular ammonia chiller unit 20 of the present disclosure, control device 34 may provide a control scheme for operation of the expansion device 28 to modulate the superheat temperature of the ammonia refrigerant at the exit of the evaporator 22 between a range of approximately 0-10 degrees F. (although other superheat temperature ranges may be used according to other embodiments). The “superheat temperature” as used in the present disclosure is understood to be the temperature of the superheated ammonia vapor refrigerant (in degrees F.) that is above the saturation temperature of the ammonia refrigerant for a particular operating pressure. For example, a superheat temperature of 10 degrees F. is intended to mean the ammonia is superheated to a temperature that is 10 degrees F. above its saturation temperature at the operating pressure. According to one embodiment, the control device 34 provides a signal to the expansion device 28 to operate the chiller unit 20 with a preferred superheat temperature within a range of approximately 6-8 degrees F. to provide for effective performance of the evaporator 22.
According to one embodiment, the control device 34 is (or comprises) a closed-loop proportional-integral-derivative (PID) controller of a type commercially available from Carel USA of Manheim, Pa., and may be programmed using appropriate proportional, integral, and/or derivative settings on the controller that may be preprogrammed, or established empirically during an initial system testing and startup operation to control the superheat setpoint within the desired temperature range. The control settings for the control device 34 may also be set to provide a lower limit for the superheat temperature range, such as a superheat temperature of approximately 1 degree F., according to one embodiment.
According to one embodiment, the control device 34 may be programmed to facilitate return of oil from the evaporator 22 to the compressor 24. For example, the control device 34 may be programmed to periodically (e.g. on a predetermined frequency) turn-off and then restart the compressor 24 as a method for periodically ensuring positive return of any soluble oil that may have accumulated in the evaporator 22 back to the compressor 24. When the compressor 24 is turned-off (e.g. intentionally for oil removal, or intermittently due to loading) the oil return valve 49 can be opened by controller 34 to return oil in the evaporator 22 to the accumulator 32 using the oil return line 47. The frequency of the shutdown-restart operation for each unit 20 may also be based upon a designation of which of the chillers is the “lead” chiller (i.e. the chiller with the most run time, as other of the chillers may be started or shutdown as needed to maintain the desired cooling capacity for the lower portion of the commercial refrigeration system). For commercial refrigeration systems that use multiple modular ammonia chiller units, the shutdown-restart operation and frequency may be established (e.g. sequenced, etc.) so that only one modular ammonia chiller unit is shutdown at any one time. Accordingly, such alternative embodiments are intended to be within the scope of this disclosure.
Referring further to the illustrated embodiment of
Still referring to
Referring still to
In the illustrated embodiment of
Referring further to
Referring now to
In some embodiments, switches 520, 530, and 560 are float switches configured to energize when the oil level is above a threshold level and de-energize when the oil level is below the threshold level. For example, compressor oil level float switch 520 may be configured to energize when the oil level in compressor 24 is above a threshold and de-energize when the oil level in compressor 24 is below the threshold. Similarly, oil reservoir level switch 530 may be configured to energize when the oil level in oil reservoir 510 is above a threshold and de-energize when the oil level in oil reservoir 510 is below the threshold. Oil drain pot level switch 560 may be configured to energize when the oil level in oil drain pot 550 is above a threshold and de-energize when the oil level in oil drain pot 550 is below the threshold.
According to some embodiments, the oil drain pot 550 receives a mixture of oil and ammonia (e.g., an oil-ammonia mixture) drained from the evaporator 22 via evaporator oil return line 552. It is understood that while oil drain pot 550 is described as receiving an oil-ammonia mixture, no ammonia may, in fact, be present in the oil-ammonia mixture. The oil drain pot level switch 560 may sense an amount of liquid ammonia and/or oil present in the oil drain pot 550. In one embodiment, the oil drain pot level switch 560 is de-energized when no liquid ammonia is present in the oil drain pot 550. For example, the oil drain pot level switch 560 may be de-energized when the oil drain pot 550 contains only oil and/or when the oil drain pot 550 is empty.
As illustrated in
The oil separation system 500 receives oil from both the evaporator 22 and the oil separator 31. The evaporator 22 includes a drain that is configured to direct oil, and, if present, ammonia from the evaporator 22 to the oil drain pot 550. Similarly, the oil separator 31 includes a drain that is configured to direct oil from the oil separator 31 to the oil separator solenoid 580 via oil separator return line 582. As previously described, all or most of any ammonia present in the oil drain pot 550 is eliminated via the oil drain pot heating loop 590. Oil from the oil drain pot 550 is directed to the oil drain pot solenoid 570 via an oil drain pot return line 572.
The oil drain pot solenoid 570 and the oil separator solenoid 580 are configured to direct oil to the oil ejector 540. The oil drain pot solenoid 570 and the oil separator solenoid 580 may be controlled according to a control scheme to direct oil in a desirable manner. The oil coming from the oil separator 31, via oil separator return line 582, may have a higher temperature and/or pressure than the oil coming from the oil drain pot 550 via oil drain pot return line 572. Accordingly, the oil from the oil separator 31 provides motive flow for the oil ejector 540 which draws oil from the oil drain pot 550 via the oil drain pot return line 572. From the oil ejector 540, oil is directed to the oil reservoir 510 via an oil ejector return line 542. Finally, the oil reservoir 510 provides oil to the compressor 24 via an oil reservoir return line 512.
According to various embodiments, the oil reservoir 510 is fluidically coupled (e.g., communicable, etc.) to the compressor 24 via the compressor oil level float switch 520. The compressor oil level float switch 520 is configured to sense a level of oil in the compressor 24 and is operable between an open state, where oil flows from the oil reservoir 510 to the compressor 24, and a closed state, where oil does not flow from the oil reservoir 510 to the compressor 24. While the compressor 24 is operating, the compressor oil level float switch 520 will bias towards the open position as needed to maintain a proper oil level in a sump portion of the compressor 24 by feeding oil from the oil reservoir 510 to the compressor 24.
The oil reservoir 510 also includes the oil reservoir level switch 530. The oil reservoir level switch 530 is positioned relative to the oil reservoir 510 such that the oil reservoir level switch 530 can sense whether the level of oil in the oil reservoir 510 is above or below a threshold (e.g., minimum) oil level. The minimum oil level may correspond to an undesirable oil level in the oil reservoir 510. When the oil in the oil reservoir 510 is at or below the minimum oil level, the oil reservoir level switch 530 is de-energized, thereby closing a contact in a circuit, shown as oil control circuit 612, and correspondingly requesting an oil charge (e.g., oil feed, oil fill, etc.). Conversely, when the oil in the oil reservoir 510 is above the minimum oil level, the oil reservoir level switch 530 is energized and the contact is open in the oil control circuit 612, and an oil charge is not requested.
As shown in
In one embodiment, the selectively control of the main equalization valve 630 and the alternate valve 640 is based on an amount of liquid ammonia in the oil reservoir 510. According to an exemplary embodiment, if ammonia is detected in the oil reservoir 510 the oil is routed to the oil drain pot 550 via the alternate oil reservoir equalization line 620 by closing the main equalization valve 630 and opening the alternate valve 640.
According to one application, the pressure within the oil drain pot 550 is greater than the suction produced by the compressor 24 and the main equalization valve 630 and the alternate valve 640 are both at least partially open. In this application, the pressure differential between the oil drain pot 550 is greater than a pressure differential between the oil reservoir 510 and the oil level float switch 520. In this application, oil is pushed into the compressor 24 by the pressure differentials.
Through the use of the alternate oil reservoir equalization line 620 a positive pressure may be created on top of the oil drain pot 550. This positive pressure may bias oil out of the oil ejector 540 when an oil feeding sequence in performed.
Referring now to
It is understood that the compressor oil level float switch 520, oil reservoir level switch 530, and oil drain pot level switch 560 may be implemented via various mechanical, electric, electromechanical, thermal, electromagnetic, and similar switches and sensors. Similarly, it is understood that various components of other embodiments may similarly be implemented in the embodiment of
According to any preferred embodiment, a commercial cascade refrigeration system 10 is provided having an upper cascade portion 12 that includes one or more compact modular ammonia chiller units 20 that provide cooling to a lower portion 18 having a low temperature CO2 subsystem 60 and/or a medium temperature chilled liquid coolant subsystem 80, where the ammonia chiller units 20 use an oil (soluble or insoluble) for lubrication of a compressor, and in some embodiments an oil management system reduces oil carryover in the ammonia from the compressor and provides positive return of any accumulated oil from the evaporator 22 back to the compressor 24.
According to the illustrated embodiment of the present disclosure, the use of critically-charged compact modular ammonia chiller units 20 to provide cascade cooling to a low temperature CO2 refrigeration subsystem 60 and a medium temperature chilled liquid coolant (e.g. glycol-water, etc.) subsystem 80 results in an all-natural refrigerant solution for use in commercial refrigeration systems, such as supermarkets and other wholesale or retail food stores or the like, that entirely avoids the use of HFC refrigerants and provides an effective and easily maintainable “green” solution to the use of HFC's in the commercial refrigeration industry. The use of relatively small, critically-charged chiller units 20 permits a series of such modular low-charge devices to be combined as necessary in an upper cascade arrangement 12 in order to cool the load from a large lower refrigeration system 18 using a naturally occurring refrigerant. In addition to being HFC-free, the system as shown and described is intended to have near-zero direct carbon emissions, one of the lowest “total equivalent warming impact” (TEWI) possible, and is intended to be “future-proof” in the sense that it would not be subject to future rules or climate change legislation related to HFCs or carbon emissions.
Referring generally to
As utilized herein, the terms “approximately,” “about,” “substantially,” and similar terms are intended to have a broad meaning in harmony with the common and accepted usage by those of ordinary skill in the art to which the subject matter of this disclosure pertains. It should be understood by those of skill in the art who review this disclosure that these terms are intended to allow a description of certain features described and claimed without restricting the scope of these features to the precise numerical ranges provided. Accordingly, these terms should be interpreted as indicating that insubstantial or inconsequential modifications or alterations of the subject matter described and claimed are considered to be within the scope of the invention as recited in the appended claims.
It should be noted that the term “exemplary” as used herein to describe various embodiments is intended to indicate that such embodiments are possible examples, representations, and/or illustrations of possible embodiments (and such term is not intended to connote that such embodiments are necessarily extraordinary or superlative examples).
The terms “coupled,” “connected,” and the like as used herein mean the joining of two members directly or indirectly to one another. Such joining may be stationary (e.g., permanent) or moveable (e.g., removable or releasable). Such joining may be achieved with the two members or the two members and any additional intermediate members being integrally formed as a single unitary body with one another or with the two members or the two members and any additional intermediate members being attached to one another.
It should be noted that the orientation of various elements may differ according to other exemplary embodiments, and that such variations are intended to be encompassed by the present disclosure.
It is important to note that the construction and arrangement of the elements of the refrigeration system provided herein are illustrative only. Although only a few exemplary embodiments of the present invention(s) have been described in detail in this disclosure, those skilled in the art who review this disclosure will readily appreciate that many modifications are possible in these embodiments (such as variations in features such as connecting structure, components, materials, sequences, capacities, shapes, dimensions, proportions and configurations of the modular elements of the system, without materially departing from the novel teachings and advantages of the invention(s). For example, any number of compact modular ammonia chiller units may be provided in parallel to cool the low temperature and/or medium temperature cases, or more subsystems may be included in the refrigeration system (e.g., a very cold subsystem or additional cold or medium subsystems). Further, it is readily apparent that variations and modifications of the refrigeration system and its components and elements may be provided in a wide variety of materials, types, shapes, sizes and performance characteristics. Accordingly, all such variations and modifications are intended to be within the scope of the invention(s).
This application is a continuation-in-part of U.S. patent application Ser. No. 13/706,122 filed Dec. 5, 2012, which is a continuation-in-part of U.S. patent application Ser. No. 12/948,442 filed on Nov. 17, 2010, the entire disclosures of which are incorporated by reference herein.
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Annex to Form PCT/ISA/206 Communication Relating to the Results of the Partial International Search, Application No. PCT/US03/34606, 2 pages. |
Number | Date | Country | |
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Number | Date | Country | |
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Parent | 13706122 | Dec 2012 | US |
Child | 15243308 | US | |
Parent | 12948442 | Nov 2010 | US |
Child | 13706122 | US |