This invention generally relates to multi-compressor refrigeration systems.
A particular example of the state of the art with respect to suction gas distribution in a parallel compressor assembly is represented by WIPO patent publication WO2008/081093 (Device For Suction Gas Distribution In A Parallel Compressor Assembly, And Parallel Compressor Assembly), which shows a distribution device for suction gas in systems with two or more compressors, the teachings and disclosure of which is incorporated in its entirety herein by reference thereto. A particular example of oil management in systems having multiple compressors is disclosed in U.S. Pat. No. 4,729,228 (Suction Line Flow Stream Separator For Parallel Compressor Arrangements), the teachings and disclosure of which is incorporated in its entirety herein by reference thereto.
Embodiments of the invention described herein represent an advancement over the current state of the art. These and other advantages of the invention, as well as additional inventive features, will be apparent from the description of the invention provided herein.
In one aspect, embodiments of the invention provide a refrigeration system that includes two or more compressors configured to compress a flow of refrigerant. The flow of refrigerant is accompanied by a flow of oil therewith. A suction flow piping arrangement is configured to supply a flow of refrigerant and oil to the two or more compressors. The suction flow piping arrangement includes a suction header configured to carry the flow of refrigerant and oil. A primary compressor supply conduit is connected to the suction header. The primary compressor supply conduit is configured to supply refrigerant and oil to a first compressor of the two or more compressors. A secondary compressor supply conduit is connected to the suction header. The secondary compressor supply conduit is configured to supply refrigerant to a second compressor of the two or more compressors. The primary compressor supply conduit is configured to supply more oil to the first compressor than the secondary compressor supply conduit supplies to the second compressor.
In a particular embodiment, the primary compressor supply conduit has an inlet port connected to the suction header and the secondary compressor supply conduit has an inlet port connected to the header. In this embodiment, the inlet port of the primary compressor supply conduit is vertically below the inlet port of the secondary compressor supply conduit. The inlet port of the primary compressor supply conduit may be arranged to form a gravitational drain as an opening at a vertical bottom location of the suction header.
In a further embodiment, the suction header has a funnel portion which reduces a diameter of the suction header and connects a larger-diameter area of the suction header with a smaller-diameter area of the inlet port for the primary compressor supply conduit.
In certain embodiments, the suction flow piping arrangement includes a return conduit upstream of the suction header and connected to an inlet of the suction header. The suction header has a distal end farthest away from the inlet. The inlet port of the primary compressor supply conduit is disposed closer to the distal end than the inlet port of the secondary compressor supply conduit.
Furthermore, the suction header has an annular wall having a circumference of 360 degrees surrounding a central passage, wherein the secondary compressor supply conduit intersects the annular wall at a side or upper portion of the annular wall such that an arc of the intersection is less than 120 degrees, wherein, during operation, oil flows along an internal surface of the annular wall, and a majority of oil bypasses the inlet port of the secondary compressor supply conduit. Preferably, this arc of the intersection ranges from 60 to 100 degrees.
In an alternate embodiment of the invention, the suction header has an annular wall surrounding a central passage, but the secondary compressor supply conduit intersects the annular wall and extends internally past the annular into the central passage via an extension segment. During operation, oil flows along an internal surface of the annular wall, and a majority of the oil bypasses the inlet port of the secondary compressor supply conduit.
In a particular embodiment, the inlet port of the primary compressor supply conduit is vertically below the inlet port of the secondary compressor supply conduit by at least one centimeter. In a further embodiment, the primary compressor supply conduit a first flow area and a flow path thereof, and the secondary compressor supply conduit defines a second flow area and a flow path thereof. The first flow path creates a pressure drop to a first compressor oil sump and the second flow path creates a pressure drop to a second compressor oil sump such that a pressure in the first compressor oil sump is from 0.1 psi to 2.0 psi greater than a pressure in the second compressor oil sump. In a more particular embodiment, the primary compressor supply conduit defines a first minimum flow area along a flow path thereof and the secondary compressor supply conduit defines a second minimum flow area along a flow path thereof. The suction header comprises a minimum flow area that is at least 1.5 times as large as the first and second minimum flow areas combined.
In at least one embodiment, the suction flow piping arrangement includes a return conduit upstream of the suction header and connected to an inlet of the suction header. The return conduit has a minimum flow area. The minimum flow area of the suction header is at least 1.4 times larger than the minimum flow area of the return conduit. The suction header has a decreased flow velocity during operation for reduced splashing of oil carried along the inner wall of the return conduit upon entry into the suction header.
The refrigeration system may include an expansion funnel segment expanding the cross-sectional flow area from the return conduit to the suction header. The refrigeration system may have a horizontal suction header, or one that is pitched at an angle between zero and five degrees from horizontal. In embodiments of the invention, the primary and secondary compressor supply conduits each have inner diameters between 25% and 75% of an inner diameter of the suction header. In more particular embodiments, the primary and secondary compressor supply conduits each have inner diameters between 45% and 55% of an inner diameter of the suction header. In certain embodiments, the primary compressor supply conduit is greater than an inner diameter of the secondary compressor supply conduit.
The refrigeration system of claim 1, wherein the secondary compressor supply conduit is configured to restrict a flow therethrough such that the flow through the secondary compressor supply conduit is less than the flow through the primary compressor supply conduit. The primary compressor supply conduit may be configured to branch off from the suction header in a vertically downward direction, while the secondary compressor supply conduit branches off from the suction header in a vertically upward direction. Alternatively, the primary compressor supply conduit may be configured to branch off from the suction header in a vertically downward direction, while the secondary compressor supply conduit branches off from the suction header in a substantially horizontal direction.
In an alternate embodiment, the primary compressor supply conduit may be configured to branch off from the suction header in a vertically downward direction, while the secondary compressor supply conduit also branches off from the suction header in a downward direction but also protrudes substantially inward into the suction header. In a more particular embodiment, the secondary compressor supply conduit protrudes into the suction header a distance equaling from 25% to 75% of the suction header inner diameter.
A flow pressure within the primary compressor supply conduit is greater than a pressure within the secondary compressor supply conduit. In a particular example, the pressure within the primary compressor supply conduit is from 0.3 psi to 1.5 psi greater than the pressure with the secondary compressor supply conduit.
In further embodiments, the refrigeration system includes a tertiary compressor supply conduit connected to the suction header, and configured to supply refrigerant and oil to a third compressor, wherein the primary compressor supply conduit is configured to supply more oil to the first compressor than the tertiary compressor supply conduit supplies to the third compressor.
In an exemplary embodiment, an oil sump pressure in the first compressor is between zero and 1.0 psi greater than an oil sump pressure in the second compressor, and wherein an oil sump pressure in the second compressor is approximately equal to the oil sump pressure in the third compressor.
In one embodiment, the flow of refrigerant and oil through the suction header reaches the primary compressor supply conduit before it reaches the secondary compressor supply conduit. In an alternate embodiment, the flow of refrigerant and oil through the suction header reaches the secondary compressor supply conduit before it reaches the primary compressor supply conduit.
In a particular embodiment, each of the two or more compressors include an opening in its compressor housing, each opening located proximate an oil sump of its respective compressor, the openings being connected via an oil sump connection, and wherein, during operation, a differential pressure exists with a higher pressure in the primary compressor to cause distribution of excess oil returned to the primary compressor to the secondary compressor through the oil sump connection.
In another aspect, embodiments of the invention provide a method of distributing oil in a multiple-compressor system. The method includes the steps of returning flow of oil and refrigerant to a suction header, and directing a flow of oil from the suction header to two or more compressors. A majority of the oil is directed to a lead compressor, and oil is distributed from the lead compressor to one or more non-lead compressors. Directing a flow of oil from the suction header to two or more compressors may include directing oil to the lead compressor via a primary compressor supply conduit, and directing oil to the one or more non-lead compressors via a secondary compressor supply conduit. The flow pressure in the primary compressor supply conduit is greater than the flow pressure in the secondary compressor supply conduit.
In a particular embodiment of the invention, the primary compressor supply conduit has an inlet positioned to form a gravitational drain at a vertical bottom location of the suction header. The secondary compressor supply conduit may include a restriction to reduce the flow of oil to its respective compressor. In particular embodiments, the restriction in the secondary compressor supply conduit is configured to create reduced suction pressure at the inlet port of its respective compressor.
The aforementioned method may also include directing oil to the lead compressor via a primary compressor supply conduit having an inlet positioned to form a gravitational drain at a vertical bottom location of the suction header. In certain embodiments, the primary compressor supply conduit branches off from the suction header in one of a downwardly vertical, downwardly angled, or horizontal direction.
The aforementioned method may further include directing oil to the one or more non-lead compressors via a secondary compressor supply conduit having an inlet positioned at a higher elevation than the inlet of the primary compressor supply conduit. In certain embodiments, the secondary compressor supply conduit branches off from the suction header in either a horizontal, upwardly vertical, or upwardly angled direction. In more particular embodiments, the secondary compressor supply conduit may branch off from the suction header in any direction, while protruding into the suction header a distance equaling from 25% to 75% of the suction header inner diameter. Additionally, the method may include returning a flow of oil and refrigerant to a suction header that is disposed horizontally, or alternatively, to a suction header that is pitched at an angle between zero and five degrees from horizontal.
Further, it is contemplated that embodiments of the invention include multi-compressor systems in which the individual compressors have different capacities. The use of a plurality of compressors in a refrigeration system, where the individual compressors have different volume indexes is disclosed in U.S. Patent Publication No. 2010/0186433 (Scroll Compressors With Different Volume Indexes and Systems and Methods For Same), filed on Jan. 22, 2010, the teachings and disclosure of which is incorporated in its entirety herein by reference thereto.
Other aspects, objectives and advantages of the invention will become more apparent from the following detailed description when taken in conjunction with the accompanying drawings.
The accompanying drawings incorporated in and forming a part of the specification illustrate several aspects of the present invention and, together with the description, serve to explain the principles of the invention. In the drawings:
While the invention will be described in connection with certain preferred embodiments, there is no intent to limit it to those embodiments. On the contrary, the intent is to cover all alternatives, modifications and equivalents as included within the spirit and scope of the invention as defined by the appended claims.
The following detailed description describes embodiments of the invention as applied in a multi-compressor refrigeration system. However, one of ordinary skill in the art will recognize that the invention is not necessarily limited to refrigeration systems. Embodiments of the invention may also find use in other systems where multiple compressors are used to supply a flow of compressed gas.
An evaporation unit 11 to provide cooling is also arranged in fluid series downstream of the condenser 7. In an alternate embodiment, the condenser 7 may feed multiple evaporation units arranged in parallel. In the embodiment of
It should be noted that, for the sake of convenience, embodiments of the invention are frequently described hereinbelow with respect to their application in systems having multiple scroll compressors for compressing refrigerant. While particular advantages and configurations are shown for scroll compressor, some of these embodiments are not limited to scroll compressors, but may find use in a variety of compressors other than scroll compressors.
An embodiment of the present invention is illustrated in
The outer housing 12 may take various forms. In a particular embodiment, the outer housing 12 includes multiple housing or shell sections, and, in certain embodiments, the outer housing 12 has three shell sections that include a central housing section 24, a top end housing section 26 and a bottom end housing section, or base plate 28. In particular embodiments, the housing sections 24, 26, 28 are formed of appropriate sheet steel and welded together to make a permanent outer housing 12 enclosure. However, if disassembly of the outer housing 12 is desired, methods for attaching the housing sections 24, 26, 28 other than welding may be employed including, but not limited to, brazing, use of threaded fasteners or other suitable mechanical means for attaching sections of the outer housing 12.
The central housing section 24 is preferably tubular or cylindrical and may abut or telescopically fit with the top and bottom end housing sections 26, 28. As can be seen in the embodiments of
In an exemplary embodiment of the invention in which a scroll compressor 14 is disposed within the outer housing 12, the scroll compressor 14 includes first and second scroll compressor bodies which preferably include a stationary fixed scroll compressor body 110 and a movable scroll compressor body 112. While the term “fixed” generally means stationary or immovable in the context of this application, more specifically “fixed” refers to the non-orbiting, non-driven scroll member, as it is acknowledged that some limited range of axial, radial, and rotational movement is possible due to thermal expansion and/or design tolerances.
The movable scroll compressor body 112 is arranged for orbital movement relative to the fixed scroll compressor body 110 for the purpose of compressing refrigerant. The fixed scroll compressor body includes a first rib 114 projecting axially from a plate-like base 116 which is typically arranged in the form of a spiral. Similarly, the movable scroll compressor body 112 includes a second scroll rib 118 projecting axially from a plate-like base 120 and is in the shape of a similar spiral. The scroll ribs 114, 118 engage with one another and abut sealingly on the respective surfaces of bases 120, 116 of the respectively other compressor body 112, 110.
In a particular embodiment of the invention, the drive unit 16 in is the form of an electrical motor assembly 40. The electrical motor assembly 40 operably rotates and drives a shaft 46. Further, the electrical motor assembly 40 generally includes a stator 50 comprising electrical coils and a rotor 52 that is coupled to the drive shaft 46 for rotation together. The stator 50 is supported by the outer housing 12, either directly or via an adapter. The stator 50 may be press-fit directly into outer housing 12, or may be fitted with an adapter (not shown) and press-fit into the outer housing 12. In a particular embodiment, the rotor 52 is mounted on the drive shaft 46, which is supported by upper and lower bearing members 42, 44.
Energizing the stator 50 is operative to rotatably drive the rotor 52 and thereby rotate the drive shaft 46 about a central axis 54. Applicant notes that when the terms “axial” and “radial” are used herein to describe features of components or assemblies, they are defined with respect to the central axis 54. Specifically, the term “axial” or “axially-extending” refers to a feature that projects or extends in a direction along, or parallel to, the central axis 54, while the terms “radial” or “radially-extending” indicates a feature that projects or extends in a direction perpendicular to the central axis 54.
In particular embodiments, the lower bearing member 44 includes a central, generally cylindrical hub 58 that includes a central bushing and opening to provide a cylindrical bearing 60 to which the drive shaft 46 is journaled for rotational support. A plate-like ledge region 68 of the lower bearing member 44 projects radially outward from the central hub 58, and serves to separate a lower portion of the stator 50 from an oil lubricant sump 76. An axially-extending perimeter surface 70 of the lower bearing member 44 may engage with the inner diameter surface of the central housing section 24 to centrally locate the lower bearing member 44 and thereby maintain its position relative to the central axis 54. This can be by way of an interference and press-fit support arrangement between the lower bearing member 44 and the outer housing 12.
As can be seen in the embodiment of
At its upper end, the drive shaft 46 is journaled for rotation within the upper bearing member 42. Hereinafter, the upper bearing member 42 is also referred to as a “crankcase”. In particular embodiments, the drive shaft 46 further includes an offset eccentric drive section 74 which typically has a cylindrical drive surface about an offset axis that is offset relative to the central axis 54. This offset drive section 74 may be journaled within a central hub 128 of the movable scroll compressor body 112 of the scroll compressor 14 to drive the movable scroll compressor body 112 about an orbital path when the drive shaft 46 rotates about the central axis 54. To provide for lubrication of all of the various bearing surfaces, the outer housing 12 provides the oil lubricant sump 76 at the bottom end of the outer housing 12 in which a suitable amount of oil lubricant may be stored.
It can also be seen that
Additionally, in particular embodiments, the suction duct 300 includes a screen 308 in the opening 304 that filters refrigerant gas as it enters the compressor through the inlet port 18, as illustrated in
As shown in
During operation, the refrigerant gas flowing into the inlet port 18 is cooler than compressed refrigerant gas at the outlet port 20. Further, during operation of the scroll compressor 14, the temperature of the motor 40 will rise. Therefore, it is desirable to cool the motor 40 during operation of the compressor. To accomplish this, cool refrigerant gas that is drawn into the compressor outer housing 12 via inlet port 18 flows upward through and along the motor 40 in order to reach the scroll compressor 14, thereby cooling the motor 40.
Furthermore, the impeller tube 47 and inlet port 78 act as an oil pump when the drive shaft 46 is rotated, and thereby pumps oil out of the lubricant sump 76 into an internal lubricant passageway 80 defined within the drive shaft 46. During rotation of the drive shaft 46, centrifugal force acts to drive lubricant oil up through the lubricant passageway 80 against the action of gravity. The lubricant passageway 80 has various radial passages projecting therefrom to feed oil through centrifugal force to appropriate bearing surfaces and thereby lubricate sliding surfaces as may be required.
A duct channel provides a fluid flow path to a drain port 330 at or near the bottom end 326 of the suction duct 234. In this embodiment, the drain port 330 extends through the bottom end 326 and thereby provides a port for draining lubricant oil into the lubricant oil sump 76, and also to communicate substantially the entire flow of refrigerant for compression to a location just upstream of the motor housing.
Not only does the suction duct 234 direct refrigerant and substantially the entire flow of refrigerant from the inlet port 18 to a location upstream of the motor 40 and to direct fluid flow through the motor 40, but it also acts as a gravitational drain preferably by being at the absolute gravitational bottom of the suction duct 234 or proximate thereto so as to drain lubricant received in the suction duct 234 into the lubricant oil sump 76. This can be advantageous for several reasons. First, when it is desirable to fill the lubricant oil sump 76 either at initial charting or otherwise, oil can readily be added through the inlet port 18, which acts also as an oil fill port so that oil will naturally drain through the suction duct 234 and into the oil sump 76 through the drain port 330. The outer housing 12 can thereby be free of a separate oil port. Additionally, the surfaces of the suction duct 234 and redirection of oil therein causes coalescing of oil lubricant mist, which can then collect within the duct channel 322 and drain through the drain port 330 back into the oil sump 76. Thus, direction of refrigerant as well as direction of lubricant oil is achieved with the suction duct 234.
During operation, the scroll compressor assemblies 10 are operable to receive low pressure refrigerant at the housing inlet port 18 and compress the refrigerant for delivery to a high pressure chamber 180 where it can be output through the housing outlet port 20. As is shown, in
Upon passing through the upper bearing member 42, the low pressure refrigerant finally enters an intake area 124 of the scroll compressor bodies 110, 112. From the intake area 124, the lower pressure refrigerant is progressively compressed through chambers 122 to where it reaches its maximum compressed state at a compression outlet 126 where it subsequently passes through a check valve and into the high pressure chamber 180. From there, high-pressure compressed refrigerant may then pass from the scroll compressor assembly 10 through the outlet port 20.
With respect to compressors #1, #2, and #3202, the internal flow of refrigerant through the compressors 202 with their isolated oil sumps 76 configuration creates a pressure drop from the suction inlet port 18 to the oil sump 76 in each of the compressors that are running, due to the restriction of the gas flow. When any of these compressors 202 is shut off and there is no flow restriction, the oil sump 76 pressure will be relatively higher than a running compressor with the same suction inlet pressure. This pressure differential between the oil sump 76 of a running compressor and the oil sump 76 of an off compressor allows for oil distribution from the off compressor to the running compressors in the refrigeration system 200, 220.
In the arrangements shown in
However, as shown in
As shown in
Referring again to
This flow can take place whether or not the lead compressor #2202 is running, as long as the oil sump pressure in the lead compressor #2202 is higher than the oil sump pressure in the receiving compressor 202. In certain embodiments, the oil will continue to be distributed in this manner until the oil sump pressures in the lead compressor #2202 and the receiving compressor(s) 202 are approximately equal. However, when either or both of the remaining compressors #1 and #3202 is not running, the increased oil sump pressure in the non-running or non-operating compressor 202 prevents oil from the lead compressor #2202 from flowing to the non-running compressor 202.
The combination of providing more oil to the lead compressor #2202 and configuring the piping to create reduced pressure at the suction inlet port 18 in the remaining compressors #1 and #3202 will result in sufficient oil distribution to all of the compressors #1, #2, and #3202 in this multiple-compressor arrangement, regardless of whether any individual compressor is on or off. This is shown in the operating matrix below in Table 1.
The above-shown matrix (Table 1) indicates how oil is distributed in the refrigeration systems of
As the refrigerant flows through the suction header 402, droplets of the entrained oil collect on the inner walls of the suction header 402. A primary compressor supply conduit 404, which branches off from the suction header 402, carries refrigerant and oil to one of the compressors 202 of the refrigeration system 200, 220 (shown in
In some cases, where both the primary compressor supply conduit 404 and the secondary compressor supply conduit 406 connect along a bottom portion of the suction header 402, the amount of oil supplied by the secondary compressor supply conduit 406 is reduced by having the inlet port for the secondary compressor supply conduit 406 protrude up into the suction header 402 farther than the inlet port for the primary compressor supply conduit 404. In other cases, this may be accomplished by connecting the inlet port for the secondary compressor supply conduit 406 at a bottom portion of the suction header 402, while connecting the inlet port for the secondary compressor supply conduit 406 along a side or top portion of the suction header 402. In the embodiments shown in
There are other ways that the primary compressor supply conduit 404 could be configured to supply a greater amount of oil to its lead compressor 202 than the secondary compressor supply conduit 406 supplies to its non-lead compressor 202, in addition to those described above. For example, in a particular embodiment, the primary compressor supply conduit 404 has a larger inner diameter than that of the secondary compressor supply conduit 406. In an alternate embodiment, such as in
In the embodiments of
Another embodiment of the invention is shown in
All references, including publications, patent applications, and patents cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
The use of the terms “a” and “an” and “the” and similar referents in the context of describing the invention (especially in the context of the following claims) is to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. The terms “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms (i.e., meaning “including, but not limited to,”) unless otherwise noted. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. Variations of those preferred embodiments may become apparent to those of ordinary skill in the art upon reading the foregoing description. The inventors expect skilled artisans to employ such variations as appropriate, and the inventors intend for the invention to be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications and equivalents of the subject matter recited in the claims appended hereto as permitted by applicable law. Moreover, any combination of the above-described elements in all possible variations thereof is encompassed by the invention unless otherwise indicated herein or otherwise clearly contradicted by context.
This patent application claims the benefit of U.S. Provisional Patent Applications Nos. 61/677,742, filed Jul. 31, 2012, and 61/677,756, filed Jul. 31, 2012, the entire teachings and disclosure of which are incorporated herein by reference thereto.
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