Patent Application
20110296859
None.
The present invention generally relates to an economizer for flash cooling a refrigerant liquid, and specifically with an economizer arranged coaxially with a condenser or other structure, e.g. an evaporator, for use in a refrigeration system having at least two stages of compression.
Refrigeration systems typically incorporate a refrigeration loop to provide chilled water for cooling a designated building space. A typical refrigeration loop includes a compressor to compress refrigerant gas, a condenser to condense the compressed refrigerant to a liquid, and an evaporator that utilizes the liquid refrigerant to cool water. The chilled water is then piped to the space to be cooled.
One such refrigeration or air conditioning system uses at least one centrifugal compressor and is referred to as a centrifugal chiller. Centrifugal compression involves the purely rotational motion of only a few mechanical parts. A single centrifugal compressor chiller, sometimes called a simplex chiller, typically range in size from 100 to above 2,000 tons of refrigeration. Typically, the reliability of centrifugal chillers is high, and the maintenance requirements are low.
Centrifugal chillers consume significant energy resources in commercial and other high cooling and/or heating demand facilities. Such chillers can have operating lives of upwards of thirty years or more in some cases.
Centrifugal chillers provide certain advantages and efficiencies when used in a building, city district (e.g. multiple buildings) or college campus, for example. Such chillers are useful over a wide range of temperature applications including Middle East conditions. At lower refrigeration capacities, screw, scroll or reciprocating-type compressors are most often used in, for example, water-based chiller applications.
One component of existing chillers is an economizer. The economizer improves the operating efficiency of the system.
An economizer is typically utilized between the condenser and the evaporator of a refrigeration system to cool refrigerant liquid below the temperature at which it leaves the condenser. Flash cooling is achieved by the evaporation of part of the refrigerant liquid as it flows from the condenser through nozzles, orifices, or other pressure reducing means into a chamber which is lower in pressure. The flashing refrigerant cools the remaining liquid by absorbing heat as it vaporizes. Upon separation from the cooled liquid, the refrigerant vapor, or flash gas, is conveyed to the inlet of a compressor stage operating at intermediate pressure. The cooled refrigerant liquid flows from the economizer to an evaporator, where it is vaporized in heat exchange relationship with another fluid, e.g., water, to satisfy a cooling load. Refrigerant vapor leaving the evaporator is typically compressed in two or more stages of compression. Prior economizers have been designed as separate units, distinct from the condenser, compressor and other structures common to chiller systems.
Prior chiller designs also typically connect the first stage discharge of a compressor to a second stage compressor and include complicated casting and piping arrangements. These designs are sometimes called two-stage, in-line designs.
Essentially, these in-line designs have a series of continuous castings that allow the discharge gas leaving a first stage compressor to be delivered into the inlet of the second stage compressor. The impeller of the first stage compressor imposes a great deal of tangential velocity to the fluid being compressed. This fluid with a tangential velocity is called swirling flow. As the fluid flows through the diffuser of the first stage compressor, it passes through a 180° U-bend. A set of blades in the return channel bend are typically used in an attempt to direct the fluid flow in an axial direction at the inlet to the second stage compressor. This swirling fluid flow is combined with the flash gas flow from the economizer to essentially inter-cool the swirling gas of the first stage compression. In practice, the mixing of the two flows is not as thorough as desired and predominately occurs far enough down the fluid flow path, e.g. in the impellers of the second stage, that only a modest efficiency improvement is gained.
According to a preferred embodiment of the present invention, a coaxial economizer for use in a chiller system comprises an inner housing and an outer housing having a common longitudinal axis. The outer housing has an inlet for receiving a fluid from an upstream compressor stage of a multistage compressor and an outlet for conveying a fluid to a downstream compressor stage of a multistage compressor. A flow chamber forms a fluid flow path about the inner housing. A flash chamber for flashing fluid in a liquid state to a gas state. A flow passage between said flash chamber and the flow chamber conveys a flashed gas from the flash chamber to the flow chamber. The flashed gas conveyed from the flash chamber and the fluid received from the inlet of the outer housing mixes along the fluid flow path toward the outlet of the outer housing.
In yet another preferred embodiment of the present invention, a method of flowing fluid through a coaxial economizer in chiller system comprises the steps of: receiving a fluid from an upstream compressor stage of a multistage compressor into a coaxial economizer; flashing a liquid to gas within a flash chamber of the coaxial economizer; passing the gas within the flash chamber through a flow passage to the flow chamber of the coaxial economizer; and mixing and flowing the gas conveyed from the flash chamber and the fluid received from the inlet of the outer housing along the fluid flow path to the outlet of the coaxial economizer. The coaxial economizer of this method comprises: an inner housing and an outer housing having a common longitudinal axis; said outer housing having an inlet for receiving a fluid from the upstream compressor stage and an outlet for conveying a fluid to a downstream compressor stage; a flow chamber forming a fluid flow path about the inner housing; a flash chamber for flashing fluid in a liquid state to a gas state; and a flow passage between said flash chamber and the flow chamber for conveying a flashed gas from the flash chamber to the flow chamber; wherein the flashed gas conveyed from the flash chamber and the fluid received from the inlet of the outer housing mix along the fluid flow path toward the outlet of the outer housing.
Embodiments of the coaxial economizer eliminates the traditional in-line design, combines multiple functions into one integrated system, improves fluid mixing of the inter-cooled gas prior to entry of the second stage and improves fluid flow dynamics (e.g. swirl reduction) through the system, which, in turn, improves chiller performance. The coaxial economizer is operable over a wide capacity range, and provides improved efficiency in a compact size.
Additional advantages and features of the invention will become more apparent from the description of a preferred embodiment of the present invention and the claims which follow.
The following figures include like numerals indicating like features where possible:
Referring to
In the embodiment depicted, chiller 20 is comprised of an evaporator 22, multi-stage compressor 24 having a non-final stage compressor 26 and a final stage compressor 28 driven by a variable speed, direct drive permanent magnet motor 36, and a coaxial economizer 40 with a condenser 44. The chiller 20 is directed to relatively large tonnage centrifugal chillers in the range of about 250 to 2000 tons or larger.
In a preferred embodiment, the compressor stage nomenclature indicates that there are multiple distinct stages of gas compression within the chiller's compressor portion. While a multi-stage compressor 24 is described below as a two-stage configuration in a preferred embodiment, persons of ordinary skill in this art will readily understand that embodiments and features of this invention are contemplated to include and apply to, not only two-stage compressors/chillers, but to single stage and other multiple stage compressors/chillers, whether in series or in parallel.
Referring to
A refrigerant in the evaporator 22 performs a cooling function. In the evaporator 22, a heat exchange process occurs, where liquid refrigerant changes state by evaporating into a vapor. This change of state, and any superheating of the refrigerant vapor, causes a cooling effect that cools liquid (typically water) passing through the evaporator tubing 48 in the evaporator 22. The evaporator tubing 48 contained in the evaporator 22 can be of various diameters and thicknesses and comprised typically of copper alloy. The tubes may be replaceable, are mechanically expanded into tube sheets, and externally finned seamless tubing.
The chilled or heated water is pumped from the evaporator 22 to an air handling unit (not shown). Air from the space that is being temperature conditioned is drawn across coils in the air handling unit that contains, in the case of air conditioning, chilled water. The drawn-in air is cooled. The cool air is then forced through the air conditioned space, which cools the space.
Also, during the heat exchange process occurring in the evaporator 22, the refrigerant vaporizes and is directed as a lower pressure (relative to the stage discharge) gas through a non-final stage suction inlet pipe 50 to the non-final stage compressor 26. Non-final stage suction inlet pipe 50 can be, for example, a continuous elbow or a multi-piece elbow.
A three-piece elbow is depicted in an embodiment of non-final stage suction inlet pipe 50 in
To condition the fluid flow distribution delivered to the non-final stage compressor 26 from the non-final stage suction inlet pipe 50, a swirl reducer or deswirler 146, as illustrated in
Generally, a multi-stage compressor compresses refrigerant gas or other vaporized fluid in stages by the rotation of one or more impellers during operation of the chiller's closed refrigeration circuit. This rotation accelerates the fluid and in turn, increases the kinetic energy of the fluid. Thereby, the compressor raises the pressure of fluid, such as refrigerant, from an evaporating pressure to a condensing pressure. This arrangement provides an active means of absorbing heat from a lower temperature environment and rejecting that heat to a higher temperature environment.
Details of the structure, function and operation of a preferred compressor assembly, which may include a mixed flow impeller and/or an inlet flow conditioning assembly, are disclosed in co-pending application Ser. Nos. ______, commonly assigned to the assignee of the present invention and are expressly incorporated herein by reference. A brief discussion of a preferred compressor assembly follows; however, other compressor assemblies may be used with embodiments of the present invention.
Referring now to
While conventional types of motors can be used with and benefit from embodiments of the present invention, a preferred motor is a permanent magnet motor 36. Permanent magnet motor 36 can increase system efficiencies over other motor types.
A preferred motor 36 comprises a direct drive, variable speed, hermetic, permanent magnet motor. The speed of the motor 36 can be controlled by varying the frequency of the electric power that is supplied to the motor 36. The horsepower of preferred motor 36 can vary in the range of about 125 to about 2500 horsepower.
The permanent magnet motor 36 is under the control of a variable speed drive 38. The permanent magnet motor 38 of an embodiment is compact, efficient, reliable, and relatively quieter than conventional motors. As the physical size of the compressor assembly is reduced, the compressor motor used must be scaled in size to fully realize the benefits of improved fluid flow paths and compressor element shape and size. Motor 36 is reduced in volume by approximately 30 to 50 percent or more when compared to conventional existing designs for compressor assemblies that employ induction motors and have refrigeration capacities in excess of 250-tons. The resulting size reduction of embodiments of the present invention provides a greater opportunity for efficiency, reliability, and quiet operation through use of less material and smaller dimensions than can be achieved through more conventional practices.
Typically, an AC power source (not shown) will supply multiphase voltage and frequency to the variable speed drive 38. The AC voltage or line voltage delivered to the variable speed drive 38 will typically have nominal values of 200V, 230V, 380V, 415V, 480V, or 600V at a line frequency of 50 Hz or 60 Hz depending on the AC power source.
The permanent magnet motor 36 comprises a rotor 68 and a stator 70. The stator 70 consists of wire coils formed around laminated steel poles, which convert variable speed drive applied currents into a rotating magnetic field. The stator 70 is mounted in a fixed position in the compressor assembly and surrounds the rotor 68, enveloping the rotor with the rotating magnetic field. The rotor 68 is the rotating component of the motor 36 and consists of a steel structure with permanent magnets, which provide a magnetic field that interacts with the rotating stator magnetic field to produce rotor torque. The rotor 68 may have a plurality of magnets and may comprise magnets buried within the rotor steel structure or be mounted at the rotor steel structure surface. The rotor 68 surface mount magnets are secured with a low loss filament, metal retaining sleeve or by other means to the rotor steel support. The performance and size of the permanent magnet motor 36 is due in part to the use of high energy density permanent magnets.
Permanent magnets produced using high energy density magnetic materials, at least 20 MGOe (Mega Gauss Oersted), produce a strong, more intense magnetic field than conventional materials. With a rotor that has a stronger magnetic field, greater torques can be produced, and the resulting motor can produce a greater horsepower output per unit volume than a conventional motor, including induction motors. By way of comparison, the torque per unit volume of permanent magnet motor 36 is at least about 75 percent higher than the torque per unit volume of induction motors used in refrigeration chillers of comparable refrigeration capacity. The result is a smaller sized motor to meet the required horsepower for a specific compressor assembly.
Further manufacturing, performance, and operating advantages and disadvantages can be realized with the number and placement of permanent magnets in the rotor 68. For example, surface mounted magnets can be used to realize greater motor efficiencies due to the absence of magnetic losses in intervening material, ease of manufacture in the creation of precise magnetic fields, and effective use of rotor fields to produce responsive rotor torque. Likewise, buried magnets can be used to realize a simpler manufactured assembly and to control the starting and operating rotor torque reactions to load variations.
The bearings, such as rolling element bearings (REB) or hydrodynamic journal bearings, can be oil lubricated. Other types of bearings can be oil-free systems. A special class of bearing which is refrigerant lubricated is a foil bearing and another uses REB with ceramic balls. Each bearing type has advantages and disadvantages that should be apparent to those of skill in the art. Any bearing type that is suitable of sustaining rotational speeds in the range of about 2,000 to about 20,000 RPM may be employed.
The rotor 68 and stator 70 end turn losses for the permanent magnet motor 36 are very low compared to some conventional motors, including induction motors. The motor 36 therefore may be cooled by means of the system refrigerant. With liquid refrigerant only needing to contact the stator 70 outside diameter, the motor cooling feed ring, typically used in induction motor stators, can be eliminated. Alternatively, refrigerant may be metered to the outside surface of the stator 70 and to the end turns of the stator 70 to provide cooling.
The variable speed drive 38 typically will comprise an electrical power converter comprising a line rectifier and line electrical current harmonic reducer, power circuits and control circuits (such circuits further comprising all communication and control logic, including electronic power switching circuits). The variable speed drive 38 will respond, for example, to signals received from a microprocessor (also not shown) associated with the chiller control panel 182 to increase or decrease the speed of the motor by changing the frequency of the current supplied to motor 36. Cooling of motor 36 and/or the variable speed drive 38, or portions thereof, may be by using a refrigerant circulated within the chiller system 20 or by other conventional cooling means. Utilizing motor 36 and variable speed drive 38, the non-final stage compressor 26 and a final stage compressor 28 typically have efficient capacities in the range of about 250-tons to about 2,000-tons or more, with a full load speed range from approximately 2,000 to above about 20,000 RPM.
With continued reference to
Preferred non-final stage compressor 26 has a compressor housing 30 having both a compressor inlet 32 and a compressor outlet 34. The non-final stage compressor 26 further comprises an inlet flow conditioning assembly 54, a non-final stage impeller 56, a diffuser 112 and a non-final stage external volute 60.
The non-final stage compressor 26 can have one or more rotatable impellers 56 for compressing a fluid, such as refrigerant. Such refrigerant can be in liquid, gas or multiple phases and may include R-123 refrigerant. Other refrigerants, such as R-134a, R-245fa, R-141b and others, and refrigerant mixtures are contemplated. Further, the present invention contemplates use of azeotropes, zeotropes and/or a mixture or blend thereof that have been and are being developed as alternatives to commonly used contemplated refrigerants.
By the use of motor 36 and variable speed drive 38, multistage compressor 24 can be operated at lower speeds when the flow or head requirements on the chiller system do not require the operation of the compressor at maximum capacity, and operated at higher speeds when there is an increased demand for chiller capacity. That is, the speed of motor 36 can be varied to match changing system requirements which results in approximately 30 percent more efficient system operation compared to a compressor without a variable speed drive. By running compressor 24 at lower speeds when the load or head on the chiller is not high or at its maximum, sufficient refrigeration effect can be provided to cool the reduced heat load in a manner which saves energy, making the chiller more economical from a cost-to-run standpoint and making chiller operation extremely efficient as compared to chillers which are incapable of such load matching.
Referring still to
The drawing of
Different arrangements and locations of the impellers 56, 58; shaft 66 and motor 36 should be apparent to one of ordinary skill in the art as being within the scope of the invention. It should be also understood that in this embodiment the structure and function of the impeller 56, impeller 58 and any other impellers added to the compressor 24 are substantially the same, if not identical. However, impeller 56, impeller 58 and any other impellers may have to provide different flow characteristics impeller to impeller.
In a preferred embodiment, fluid is delivered from the impellers 56, 58 and diffusers 112 to a non-final stage external volute 60 and a final stage external volute 62, respectively for each stage. The volutes 60, 62, illustrated in
The external volutes 60, 62 of this embodiment replace the conventional return channel design and are comprised of two portions—the scroll portion and the discharge conic portion. Use of volutes 60, 62 lowers losses as compared to return channels at part load and have about the same or less losses at full load. As the area of the cross-section increases, the fluid in the scroll portion of the volutes 60, 62 is at about a constant static pressure so it results in a distortion free boundary condition at the diffuser exit. The discharge conic increases pressure when it exchanges kinetic energy through the area increase.
In the case of the non-final stage compressor 26 of this embodiment, fluid is delivered from the external volute 60 to a coaxial economizer 40. In the case of the final stage compressor 28 of this embodiment, the fluid is delivered from the external volute 62 to a condenser 44 (which may be arranged coaxially with an economizer).
Turning now to the coaxial economizer 40, the coaxial economizer 40 has an economizer 42 arranged coaxially with a condenser 44. Applicants refer to this arrangement as an exemplary coaxial economizer 40. The coaxial economizer 40 combines multiple functions into one integrated system and further increases system efficiencies. Coaxial is used in the common sense where one structure (e.g. economizer 42) has a coincident axis with at least one other structure (e.g. the condenser 44 or evaporator 22). A discussion of a preferred coaxial economizer 40 follows.
By the use of coaxial economizer 40, additional efficiencies are added to the compression process that takes place in chiller 20 and the overall efficiency of chiller 20 is increased. The coaxial economizer 40 combines multiple functions into one integrated system and further increases system efficiencies.
Other coaxial economizer arrangements within the scope of this invention should be apparent. For example, while economizer 42 surrounds and is coaxial with condenser 44 in a preferred embodiment, it will be understood by those skilled in the art that it may be advantageous in certain circumstances for economizer 42 to surround evaporator 22. An example of such a circumstance is one in which, due to the particular application or use of chiller 20, it is desired that evaporator 22, when surrounded by economizer 42, acts, in effect, as a heat sink to provide additional interstage cooling to the refrigerant gas flowing through economizer 40, prospectively resulting in an increase in the overall efficiency of the refrigeration cycle within chiller 20.
As illustrated in
The economizer 40 preferably has two chambers: a flow chamber forming a fluid flow path about the inner housing and a economizer flash chamber 158 for flashing fluid in a liquid state to a gas state. In one embodiment, the economizer 40 has two chambers isolated by two spiraling baffles 154. The number of baffles 154 may vary. The baffles 154 isolate an economizer flash chamber 158 and a superheat chamber 160.
The economizer flash chamber 158 contains two phases of fluid, a gas and a liquid. The condenser 44 supplies liquid to the economizer flash chamber 158.
The spiraling baffles 154 depicted in
During operation, gas in the economizer flash chamber 158 is drawn out through the injection slots 156 into the superheat chamber 160. The spiraling baffles 154 are oriented so that the fluid exits through the two injection slots 156 of the spiraling baffles 154. The fluid exits in approximately the same tangential directions as the flow discharged from the non-final stage compressor 26. The face areas of the flow passage 156 are sized to produce approximately matching velocities and flow rates in the flow passage 156 relative to the adjacent local mixing superheat chamber 160 (suction pipe side). This requires a different injection face area of the flow passage 156 based on the location of the tangential discharge conic flow, where a smaller gap results closest to the shortest path length distance, and a larger gap at the furthest path length distance. Intermediate superheat chambers 160 and flash chambers may be provided, for example, when more than two stages of compression are used.
The economizer flash chamber 158 introduces approximately 10 percent (which can be more or less) of the total fluid flow through the chiller 20. The economizer flash chamber 158 introduces lower temperature economizer flash gas with superheated gas from the discharge conic of the non-final stage compressor 26. The coaxial economizer 42 arrangement generously mixes the inherent local swirl coming out of the economizer flash chamber 158 and the global swirl introduced by the tangential discharge of the non-final stage compressor 26—discharge which, in one embodiment, is typically over the top of the outside diameter condenser 44 and the inside diameter of coaxially arranged economizer 42.
The liquid in chamber 162 is delivered to the evaporator 22. This liquid in the bottom portion of the economizer flash chamber 158 is sealed from the superheat chamber 160. Sealing of liquid chamber 162 can be sealed by welding the baffle 154 to the outer housing of the coaxially arranged economizer 42. Leakage is minimized between other mating surfaces to less than about 5 percent.
In addition to combining multiple functions into one integrated system, the coaxial economizer 40 produces a compact chiller 20 arrangement. The arrangement is also advantageous because the flashed fluid from the economizer flash chamber 158 better mixes with the flow from the non-final stage compressor 26 than existing economizer systems, where there is a tendency for the flashed economizer gas not to mix prior to entering a final stage compressor 28. In addition, the coaxial economizer 40 dissipates local conic discharge swirl as the mixed out superheated gas proceeds circumferentially to the final stage compressor 28 to the tangential final stage suction inlet 52. Although some global swirl does exist at the entrance to the final stage suction pipe 52, the coaxial economizer 40 reduces the fluid swirl by about 80 percent compared to the non-final stage compressor 26 conic discharge swirl velocity. Remaining global swirl can be optionally reduced by adding a swirl reducer or deswirler 146 in the final stage suction pipe 52.
Turning to
From the coaxial economizer 40 of this embodiment, the refrigerant vapor is drawn by final stage impeller 58 of the final stage compressor 28 and is delivered into a conformal draft pipe 142. Referring to
Conformal draft pipe 142 can have multiple legs. Use of multiple legs may be less costly to produce than a conformal draft pipe 142 as depicted in
Referring still to
Optionally, a swirl reducer or deswirler 146 may be positioned within the final stage suction pipe 52. Details of the structure, function and operation of a preferred swirl reducer 146 are disclosed in co-pending application Ser. Nos. ______, commonly assigned to the assignee of the present invention and are expressly incorporated herein by reference. A brief discussion of a preferred swirl reducer 146 follows; however, other swirl reducers may be used with embodiments of the present invention.
The swirl reducer 146 may be positioned in the first leg 52A, second leg 52B, or third leg 52C. Referring to
The number of chambers 152 is set by the amount of swirl control desired. More chambers and more blades produce better deswirl control at the expense of higher blockage. In one embodiment, there are four radial blades 150 that are sized and shaped to turn the tangential velocity component to axial without separation and provide minimum blockage.
The location of the swirl reducer 146 may be located elsewhere in the suction pipe 52 depending on the design flow conditions. As indicated above, the swirl reducer 146 may be placed in the non-final stage suction pipe 50 or final stage suction pipe 52, in both said pipes, or may not be used at all.
Also, the outside wall of the swirl reducer 146 can coincide with the outside wall of the suction pipe 52 and be attached. Alternatively, the one or more flow conduits 148 and one or more radial blades 150 can be attached to an outside wall and inserted as a complete unit into suction pipe 50, 52.
As illustrated in
The radial uncambered portion of the radial blade 150 (no geometric turning) is trapped by the concentric flow conduits 148 at about sixty percent of the chord length of the radial blade 150. The refrigerant exits the swirl reducer 146 positioned in the final stage suction pipe 52 and is further drawn downstream by the final stage compressor 28. The fluid is compressed by the final stage compressor 28 (similar to the compression by the non-final stage compressor 26) and discharged through the external volute 62 out of a final stage compressor outlet 34 into condenser 44. Referring to
Turning now to the condenser 44 illustrated in
The heat extracted from the refrigerant is either directly exhausted to the atmosphere by means of an air cooled condenser, or indirectly exhausted to the atmosphere by heat exchange with another water loop and a cooling tower. The pressurized liquid refrigerant passes from the condenser 44 through an expansion device such as an orifice (not shown) to reduce the pressure of the refrigerant liquid.
The heat exchange process occurring within condenser 44 causes the relatively hot, compressed refrigerant gas delivered there to condense and pool as a relatively much cooler liquid in the bottom of the condenser 44. The condensed refrigerant is then directed out of condenser 44, through discharge piping, to a metering device (not shown) which, in a preferred embodiment, is a fixed orifice. That refrigerant, in its passage through metering device, is reduced in pressure and is still further cooled by the process of expansion and is next delivered, primarily in liquid form, through piping back into evaporator 22 or economizer 42, for example.
Metering devices, such as orifice systems, can be implemented in ways well known in the art. Such metering devices can maintain the correct pressure differentials between the condenser 42, economizer 42 and evaporator 22 of the entire range of loading.
In addition, operation of the compressors, and the chiller system generally, is controlled by, for example, a microcomputer control panel 182 in connection with sensors located within the chiller system that allows for the reliable operation of the chiller, including display of chiller operating conditions. Other controls may be linked to the microcomputer control panel, such as: compressor controls; system supervisory controls that can be coupled with other controls to improve efficiency; soft motor starter controls; controls for regulating guide vanes 100 and/or controls to avoid system fluid surge; control circuitry for the motor or variable speed drive; and other sensors/controls are contemplated as should be understood. It should be apparent that software may be provided in connection with operation of the variable speed drive and other components of the chiller system 20, for example.
It will be readily apparent to one of ordinary skill in the art that the centrifugal chiller disclosed can be readily implemented in other contexts at varying scales. Use of various motor types, drive mechanisms, and configurations with embodiments of this invention should be readily apparent to those of ordinary skill in the art. For example, embodiments of multi-stage compressor 24 can be of the direct drive or gear drive type typically employing an induction motor.
Chiller systems can also be connected and operated in series or in parallel (not shown). For example, four chillers could be connected to operate at twenty five percent capacity depending on building load and other typical operational parameters.
The patentable scope of the invention is defined by the claims as described by the above description. While particular features, embodiments, and applications of the present invention have been shown and described, including the best mode, other features, embodiments or applications may be understood by one of ordinary skill in the art to also be within the scope of this invention. It is therefore contemplated that the claims will cover such other features, embodiments or applications and incorporates those features which come within the spirit and scope of the invention.
This application is a continuation of U.S. application Ser. No. 12/034,551, filed Feb. 20, 2008, the contents of which are incorporated by reference in their entirety.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 12034551 | Feb 2008 | US |
| Child | 13154703 | US |
