This is the US national stage of International Application No. PCT/US06/62774, filed Dec. 31, 2006.
The invention relates to compressors. More particularly, the invention relates to compressor capacity control.
In the refrigeration compressor art, one broad class of compressors is reciprocating piston compressors. Each of one or more pistons is reciprocally mounted in an associated cylinder. Reciprocation of the piston displaces a given volume of the cylinder to act as a compressor or pump.
In applications requiring small displacement volume and/or high pressures, it is known to use a stepped piston configuration. Such configurations are often termed “crosshead pistons”. A relatively small cross-sectional area distal portion of the piston is accommodated in an associated portion of the cylinder. A relatively large cross-sectional area proximal portion may be sized for appropriately robust engagement with an appropriately sized connecting rod. An example of such a configuration is shown in US Patent Application Publication 2005/0129543 A1.
In such a crosshead configuration, the proximal region of the cylinder is typically vented to the compressor sump and is not used for compression. However, one prior proposal to use the proximal area for compression is found in U.S. Pat. No. 5,716,197.
Accordingly, one aspect of the invention involves a compressor having a housing. A crank is carried by the housing for rotation about a crank axis. A cylinder is defined within the housing and has a proximal portion and a distal portion. The distal portion is smaller in transverse cross-sectional area than is the proximal portion. A piston is held within the housing for reciprocal movement at least partially within the cylinder. The piston also has a distal portion smaller in transverse cross-sectional area than a proximal portion. A connecting rod is pivotally coupled to the crank for relative rotation about a proximal axis and to the piston for relative rotation about a distal axis. A first compression chamber exists in the cylinder distal portion beyond the end of the piston. A second compression chamber exists in the cylinder proximal portion beyond a piston shoulder. The first and second compression chambers are non-series and non-parallel.
In various implementations, a first inlet valve and a first outlet valve may be positioned along the first chamber. A second inlet valve and a second outlet valve may be positioned along the second chamber. At least one additional cylinder may be defined within the housing and has a single chamber. The second inlet valve and the second outlet valve may be positioned along the shoulder of the cylinder. A controller may be configured to control operation of the compressor in each of first and second modes of operation. In the first mode, the compressor compresses flow along a first flowpath segment through the first chamber but not a second flowpath segment through the second chamber. In the second mode, the compressor compresses flow along both the first and second flowpath segments. The compressor may be used with a carbon dioxide-based refrigerant. The compressor may be used to drive a dual economizer refrigeration system.
The details of one or more embodiments of the invention are set forth in the accompanying drawings and the description below. Other features, objects, and advantages of the invention will be apparent from the description and drawings, and from the claims.
Like reference numbers and designations in the various drawings indicate like elements.
The exemplary compressor is a reciprocating compressor wherein the housing defines a plurality of cylinders. Each cylinder accommodates an associated piston. Exemplary multi-cylinder configurations include: in-line; vee; and horizontally opposed. The exemplary compressor includes three cylinders 30, 31, and 32.
Each cylinder has a central axis 502 parallel to which an outward (distal) direction 504 is defined. Pistons 33, 34, and 35 are mounted at least partially in the associated cylinders 30, 31, and 32. Each piston is guided by its cylinder for relative motion in the outward direction 504 and back. As is discussed below, the exemplary cylinders 30 and 31 and pistons 33 and 34 are conventional non-stepped cylinders and pistons. Each of these two piston/cylinder combinations thus defines a single respective associated chamber or compression volume 36 and 37. As is discussed further below, the cylinder 32 and piston 35 are stepped to define two chambers or volumes.
As the motor rotates the crankshaft about its axis 500, the crank portion 45 and connecting rod 44 cooperate to reciprocally drive the piston between a topped position of
A first suction valve 100 and a first discharge valve 102 are positioned in the top surface 56 of the distal chamber 70 to selectively place the distal chamber in respective communication with a first suction location 104 and a first discharge location 106. Depending upon implementations, the suction and discharge locations 104 and 106 may be respective suction and discharge plenums. The exemplary valves 100 and 102 are poppet valves mounted along the head surface. The valves may be synchronized to the crankshaft (e.g., via mechanical or electronic means) to permit the compressor to pump a working fluid from the suction location to the discharge location or may be self-actuated by pressure differences between the distal chamber 70 and the respective suction and discharge locations 104 and 106. Exemplary self-actuated valves are free-floating or have a light spring pressure biasing them closed. They will remain closed with a pressure difference across them in one direction but will open with a small pressure difference in the other direction (i.e., the desired direction of flow). They may thus essentially be very fast-acting check valves. To maintain isolation of the distal chamber, the piston distal portion may carry one or more first sealing rings 110 positioned to sealingly engage with the cylinder sidewall distal surface 52 during the reciprocal movement of the piston.
According to the present invention, the proximal chamber 72 may also be used to provide an associated trapped volume for compressor use. In an exemplary implementation of this, the piston proximal portion is similarly sealed to the cylinder sidewall proximal surface (e.g., via one or more second sealing rings 114 carried along the piston proximal portion similar to rings of the other pistons). A second set of valves is positioned along the second chamber. The exemplary second set of valves includes a suction valve 120 and a discharge valve 122. The exemplary suction and discharge valves are also poppet valves mounted along the cylinder shoulder surface to selectively place the proximal chamber in respective communication with a second suction location 124 and a second discharge location 126 and are synchronized to the camshaft rotation or may be self-actuated as discussed above.
Various connection/operational implementations of the two-chamber cylinder are possible. The two chambers may be operated in parallel with each other. For example, the suction locations may be part of a common suction plenum and the discharge locations may be part of a common discharge plenum. The two may be operated in series with each other (e.g., one of the suction locations is coupled to one of the discharge locations). Via appropriate valves, the system may be configured to switch between parallel and series operation. Via appropriate valves and/or control of the suction and discharge valves, one or both of the chambers may be disabled from compression to provide a capacity control.
By presenting one or more stepped cylinder/piston combinations and one or more non-stepped combinations in a single compressor, advantageous flexibility of operation may be obtained at reasonable cost. The use of such a compressor also facilitates refrigeration systems that may make use of the compressor's operational flexibility.
In a normal operating condition, a recirculating flow of refrigerant passes along the primary flowpath 204, being compressed in the first and second cylinders 30 and 31. The compressed refrigerant is cooled in the gas cooler/condenser 206, expanded in the first expansion device 212, and then heated in the evaporator 214. In an exemplary implementation, the gas cooler/condenser 206 and evaporator 214 are refrigerant-air heat exchangers with associated fan-forced air flows. The evaporator 214 may be in the refrigerated space or its airflow may pass through the refrigerated space. Similarly, the gas cooler/condenser 206 or its airflow may be external to the refrigerated space.
The exemplary system 200 includes a first economizer flowpath 220. The first economizer flowpath 220 branches from the primary flowpath at a location/condition 222 between the gas cooler/condenser outlet and first economizer inlet. The exemplary first economizer flowpath 220 returns to the refrigerant primary flowpath at a location/condition 224 between the first 30 and second 31 cylinders (e.g., at their respective outlet/discharge and inlet/suction conditions/locations). The first economizer flowpath 220 passes sequentially through a second expansion device 226, then the first economizer 208, and then a valve 228. A leg 230 of the first economizer flowpath 220 in the first economizer 208 is in heat transfer relation with a leg 232 of the refrigerant primary flowpath 204 within the first economizer 208. Thus, when the first economizer flowpath is active, refrigerant flow along the first economizer flowpath cools the refrigerant in the refrigerant primary flowpath in the first economizer.
The exemplary system 200 also includes a second economizer flowpath 240. The second economizer flowpath 240 branches from the primary flowpath 204 at a condition/location 242 between the first and second economizers. The second economizer flowpath 240 returns to the primary flowpath 204 at a condition/location 244 between the second cylinder 31 and the gas cooler/condenser 206. The second economizer flowpath 240 proceeds sequentially through a third expansion device 246, the second economizer 210, a valve 248, and one of the two chambers 70 and 72 of the stepped cylinder 32. Thus, when the second economizer flowpath is active, refrigerant flow along the second economizer flowpath cools the refrigerant in the refrigerant primary flowpath in the second economizer.
The exemplary system 200 also includes a branch flowpath 260. The branch flowpath 260 branches from the primary flowpath 204 between the evaporator outlet and first cylinder inlet (e.g., at the suction condition/location 202). The branch flowpath 260 passes sequentially through a valve 262 and the other of the two chambers of the stepped cylinder (e.g., 72 in the implementation), to rejoin the primary flowpath 204 between the second cylinder and gas cooler/condenser (e.g., at the condition/location 244). Additional system components and further system variations are possible.
The exemplary expansion devices 212, 226, and 246 may be fixed expansion devices, thermomechanically controlled expansion devices, or system-controlled expansion devices. For example, in various implementations, the first expansion device 212 may be an electronic expansion valve controlled by a control system 280 which may also control operation of the compressor, other valves, fans, and the like. The expansion devices 246 and 226 may be similar or may be fixed orifices. Alternatively, the devices may be thermal expansion valves with control bulbs appropriately mounted in the system. Exemplary valves 228 and 248 may be simple on-off valves, electronically controlled by the control system 280. The valve 262 may be similar or may be an adjustable valve to control a flow rate along the branch flowpath 260. The valve 262 may be positioned in the compressor as a suction cut-off valve at the compression chamber 72.
An exemplary implementation involves a system using CO2 (R-744) as a refrigerant. Potential applications include transport refrigeration units (e.g., truck boxes, trailers, cargo containers, and the like) which require broad capabilities. A given unit configuration may be manufactured for multiple operators with different needs. Many operators will have the need to, at different times, use a given unit for transport of frozen goods and non-frozen perishables. An exemplary frozen goods temperature is about −10° F. or less and an exemplary non-frozen perishable temperature is 34-38° F. The operator will predetermine appropriate temperature for each of the two modes. Prior to a trip or series, the technician or driver will enter the appropriate one of the two temperatures. Other operators may have broader requirements (e.g., an exemplary overall range of −40-57° F.).
In operation, the first economizer flowpath 220 may be operated by the valve 228 to run the first economizer 208 as is well known in the art. Similarly, the valve 248 may be used to provide further economizer function. The valve 262 may be operated as a suction cutoff valve to its associated chamber of the stepped cylinder. When open, the valve 262 allows the associated chamber of the stepped cylinder to provide additional capacity to the system.
The operation of the valves 228, 248 and 262 depend on the controlled and ambient conditions and on the modes of operation. In an exemplary embodiment, the valves 226, 246, and 212 directly regulate flow based on a sensed parameter of the cycle. The valves 228 and 248 regulate the economization of the cycle under control of the controller 280. If either of valves 228 and 248 are open they improve the efficiency and capacity of the system. In an exemplary implementation, the valves 228 and 248 may be kept closed during system startup to prevent overloading of the compressor. The valves 228 and 248 may also be kept closed when a low capacity is required (e.g., a relatively high desired temperature of the cooled space such as in a non-frozen perishable cargo mode). When there is a requirement of additional capacity of the system like during pulldown or high controlled temperature condition or during a hot day the valve 262 is opened. Opening the valve 262 increases the refrigerant mass flow through evaporator, thereby increasing capacity. In systems where capacity improvement or adjustments are needed in precise amounts a modulating valve may be used for 262 and its operation modulated.
Various possible valve state combinations are shown in Table I below.
Subtle optimization considerations may differentiate between the choice of combination #2 vs. #3 and #6 vs. #7. The system may, however be configured via selection of economizer heat exchanger size and cylinder/chamber size to increase the differentiation between the combinations and their associated situations. Selection between the combinations may be made by the controller responsive to a combination pf pre-programming, user-set parameters, sensed parameters, and/or calculated parameters (e.g., current draws). Other factors that may influence the particular combination include compressor balance or vibration control.
In engineering the compressor, the displacements of the two chambers of the stepped cylinder and their respective compression ratios or volume indices may be selected for a variety of purposes. For example, the volume indices may be associated with the anticipated required pressure differences. The displacements may then be selected based upon desired relative flow rates. In one example, the volume indices are each the same as those of the non-stepped cylinders. This allows either of the chambers to conveniently be operated in parallel with the other cylinders. Alternatively, the volume indices may be greater than that of the other cylinders individually but equal to or less than the effective series combination of the other cylinders. This allows the chamber(s) to be operated in parallel with the series combination of the other cylinders.
The relative sizes of the cylinders/chambers 30, 31, and 70 help control the pressures in the flowpaths 220 and 240 relative to the evaporator and gas cooler/condenser pressures and thereby help optimize the efficiency of the system. However, the actual sizes of the cylinders/chambers 31, 32, 70, and 72 determine the capacity of the system. In an exemplary implementation, the first cylinder 30 is bigger than the second cylinder 31, which in turn is bigger than the chamber 70. The size of chamber 72 may merely be what is effectively available in view of the selected size of the chamber 70. The pressure ratios of the various cylinders/chambers may reflect desired performance issues.
One or more embodiments of the present invention have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the invention. For example, when implemented in the reengineering of an existing compressor configuration or remanufacturing of an existing compressor, details of the baseline configuration may influence or dictate details of any particular implementation. Accordingly, other embodiments are within the scope of the following claims.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2006/062774 | 12/31/2006 | WO | 00 | 6/25/2009 |
Publishing Document | Publishing Date | Country | Kind |
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WO2008/082410 | 7/10/2008 | WO | A |
Number | Name | Date | Kind |
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1417571 | Riesner | May 1922 | A |
2205793 | Hunt | Jun 1940 | A |
4974427 | Diab | Dec 1990 | A |
5674053 | Paul et al. | Oct 1997 | A |
5716197 | Paul et al. | Feb 1998 | A |
7096681 | Wills et al. | Aug 2006 | B2 |
20050129543 | Collings | Jun 2005 | A1 |
20050262859 | Crane et al. | Dec 2005 | A1 |
Number | Date | Country |
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1366929 | Jul 1964 | FR |
Number | Date | Country | |
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20100095690 A1 | Apr 2010 | US |