AU2005327580B2

AU2005327580B2 - Compressor system with controlled lubricant reclaim

Info

Publication number: AU2005327580B2
Application number: AU2005327580A
Authority: AU
Inventors: Cornelius Holmes
Original assignee: Carrier Corp
Current assignee: Carrier Corp
Priority date: 2005-02-15
Filing date: 2005-02-15
Publication date: 2010-10-21
Anticipated expiration: 2025-02-15
Also published as: EP1851491B1; AU2005327580A1; CN100538216C; EP1851491A4; WO2006088459A3; WO2006088459A2; EP1851491A2; HK1120599A1; CN101180507A; US20080271477A1

Description

WO 2006/088459 PCT/US2005/005092 COMPRESSOR SYSTEM WITH CONTROLLED LUBRICANT RECLAIM BACKGROUND OF THE INVENTION [0001] The invention relates to compressor systems and, more particularly, the invention relates to a system and method for controlled recovery of lubricant for such systems. [0002] Compressors, for example screw compressors, are commonly used in various applications including, for example, water-cooled chillers. [0003] A typical compressor requires oil to lubricate bearings, seals, gaps between rotors and between the rotors and adjacent stationary components such as the housing and end plates, and the like. [0004] The bearing load carrying capacity depends heavily upon oil viscosity. Further, the sealing characteristics of the oil are dependent upon viscosity. [0005] The oil to provide such sealing and lubrication is typically circulated through the system along with refrigerant. Oil entrained with the refrigerant is circulated from the compressor discharge through the system. [0006] Separation and recycle of this oil, while maintaining acceptable oil viscosity, is a pressing need in the industry. [0007] It is therefore a primary object of the present invention to provide a system and method whereby recovery of the oil and desired viscosity levels are efficiently accomplished and maintained. [0008] Other objects and advantages of the present invention will appear herein below. 1 SUMMARY OF THE INVENTION [0009] In accordance with the present invention, the foregoing objects and advantages have been readily attained. [00101 According to the invention, a compressor system with controlled lubricant reclaim is provided, which system comprises a compressor circuit comprising a compressor, condenser and an evaporator connected by refrigerant flow lines; a lubricant circuit for circulating lubricant to the compressor; a reclaim vaporizer adapted to heat a refrigerant-lubricant mixture from the evaporator whereby the mixture is heated and lubricant and refrigerant are separated to provide reclaimed lubricant to the lubricant circuit and reclaimed refrigerant to the compressor circuit; and a control unit adapted to control flow of the mixture from the evaporator to the reclaim vaporizer based upon temperature of the mixture from the evaporator and temperature of reclaimed lubricant leaving the reclaim vaporizer. [0011] In further accordance with the invention, a method is provided for controlling reclaim of lubricant in a compressor system, which method comprises the steps of operating a compressor circuit comprising a compressor, condenser and an evaporator and a lubricant circuit for circulating lubricant to the compressor so as to provide a refrigerant-lubricant mixture leaving the evaporator; exposing the mixture to heat in a reclaim vaporizer so as to provide reclaimed lubricant to the lubricant circuit and reclaimed refrigerant to the compressor circuit; and controlling flow rate of the mixture to the reclaim vaporizer based upon temperature of the mixture leaving the evaporator and temperature of the reclaimed lubricant leaving the reclaim vaporizer. [0012] By controlling the rate of exposure of refrigerant lubricant mixture to heat, control of the resulting lubricant viscosity is advantageously accomplished. 2 BRIEF DESCRIPTION OF THE DRAWINGS [0013] A detailed description of preferred embodiments of the present invention follows, with reference to the attached drawings wherein: [0014] Figure 1 schematically illustrates a preferred system and method in accordance with the present invention. DETAILED DESCRIPTION [0015] The invention relates to a system and method for controlled recovery of lubricant such as oil in a compressor system whereby resulting viscosity of the oil can be controlled and maintained. [0016] Figure 1 shows a system 10 in accordance with the present invention. This basic system, without the additional features disclosed herein, is the subject of commonly owned U.S. Patent No.. 6,672,102 to Huenniger et al. issued January 6, 2004. This patent is incorporated herein by reference. [0017] Referring to Figure 1 herein, system 10 includes a compressor circuit including a compressor 12, a condenser 14 and an evaporator 16 which are connected by refrigerant lines 18, 20 for flow of refrigerant-through these components as desired. A typical system includes a further flow line from condenser 14 through an expansion device (not shown) and to evaporator 16. These components and lines complete a typical compressor circuit. [0018] In further accordance with the invention, a lubricant circuit is provided for conveying oil from an oil sump 22 through an oil pump 24 and to an oil inlet 26 of compressor 12. A filter 28 can be positioned along oil line 30, if desired. An oil drain 32 carries oil from compressor 12 back to oil sump 22. (0019] As set forth above, during operation of the compressor circuit and lubricant circuit, oil or other suitable lubricant is mixed with refrigerant discharged 3 WO 2006/088459 PCT/US2005/005092 through line 18 to condenser 14, the expansion device and evaporator 16. Separation and reclaim of the oil for further use within the system, while maintaining oil viscosity at desired values, is the focus of the present invention. [0020] According to the invention, the mixture within evaporator 16 is therefore metered or fed to a reclaim vaporizer 34, wherein the mixture is exposed to heat so as to separate the refrigerant from the lubricant. This heat boils the refrigerant off from the lubricant, and the refrigerant passes through vent lines 36 back to line 20 and to the suction inlet 38 of compressor 12. Due to the control of the present invention, remaining oil has at this point been sufficiently purged of refrigerant as to have a viscosity suitable to maintain sealing and lubrication of the compressor as desired. [0021] Note that a vent line 38 is also communicated with oil sump 22 for carrying any further boiled off refrigerant from this location back to suction inlet 38 as well. [0022] Oil separated within reclaim vaporizer 34 passes through an oil discharge line 40 and back to sump 22 for further circulation within the lubricant circuit. [0023] In accordance with the invention, heat is preferably applied to the refrigerant-lubricant mixture within vaporizer 34 from hot gas from the discharge of compressor 12, which can be fed to vaporizer 34, for example through line 42 which advantageously is separated off of main line 18 upstream of condenser 14. This hot gas from compressor 12 will be at a temperature greater than the temperature of the mixture of refrigerant and lubricant within evaporator 16. Thus, the gas discharge from compressor 12 can advantageously be used to provide heat to the mixture, and the resulting cooled refrigerant is then passed through line 44 to evaporator 16 and back to suction inlet 38 of compressor 12. 4 WO 2006/088459 PCT/US2005/005092 [0024] Under certain operating conditions, sufficient heat may not be provided from the gas discharge of compressor 12. To this end, the system in accordance with the present invention may further preferably include a supplemental heat source 46, which is schematically shown in the drawings, and which can be a heater device and/or a further flow of fluid from the system, either of which can be controlled to provide additional heat to vaporizer 34 as needed. [0025] In accordance with the present invention, it has been found that the viscosity of lubricant circulating within the lubricant circuit can be controlled by controlling the rate of separation of refrigerant from the lubricant within vaporizer 34. To this end, a control valve 48 is advantageously positioned along line 50 for carrying the mixture from evaporator 44 to reclaim vaporizer 34. This valve 48 is advantageously adapted to be controlled by a control unit 50 which includes sensors of the mixture temperature (Tref), for example within evaporator 44, and the temperature of reclaimed oil (Toil) , for example within line 40 to sump 22. [0026] It has been found that the temperature differential between Toil and Tref is directly proportional to the resulting viscosity of this separated oil. Thus, control unit 50 can advantageously be adapted to sense or otherwise determine these temperatures, and then operate control valve 48 so as to control flow rate of the mixture from evaporator 16 to reclaim vaporizer 34 and thereby control the temperature difference between Toil and Tref. In accordance with the present invention, a pre-selected range of temperature difference can be entered into control unit 50 and control unit 50 can be adapted or otherwise programmed to control valve 48 so as to maintain the temperature difference within this pre-selected range. 5 WO 2006/088459 PCT/US2005/005092 [0027] As the flow rate of mixture from evaporator 16 is increased, the amount of refrigerant boiled off within reclaim vaporizer 34 per flow volume will decrease, and the viscosity of resulting separated lubricant will be reduced. As the flow rate of mixture from evaporator 16 is decreased, further separation is accomplished per flow volume by the heat applied thereto, and the resulting separated lubricant will contain less refrigerant and have a higher viscosity. [0028] Control unit 50 can be any suitable processor unit programmed with proper command instructions as set forth above. Specifically, control unit 50 is preferably adapted to receive signals that are indicative of the temperatures Toil and Tref, and to utilize these signals to determine a proper operating position for valve 48. [0029] It should readily be appreciated that the system and method in accordance with the present invention could readily be accomplished through other approaches as well. Specifically, it is considered to be well within the scope of the present invention to control resulting viscosity of separated lubricant by instead controlling the amount of heat applied within vaporizer 34, and/or controlling both the amount of heat and the flow rate through valve 48 as described above. [0030] Also as shown in Figure 1, supplemental heater 46, if needed, is further advantageously controlled by control unit 50. Such control would involve control unit 50 receiving the sensed signal related to temperatures Toil and Tref, and would be programmed under situations where the difference between these temperatures is insufficient and valve 48 cannot be further closed to operate supplemental heater 46 to apply further heat as desired. [0031] It should readily be appreciated that while portions of the above disclosure refer to the lubricant as oil, the system of the present invention is readily applicable to 6 WO 2006/088459 PCT/US2005/005092 systems utilizing other fluids as lubricant as well, so long as this other lubricant is to be separated from refrigerant with which it is mixed during operation of the compressor and lubricant circuits. [0032] It should also be appreciated that while this disclosure is made in terms of a screw compressor, the system and method of the present invention are readily applicable to any type of compressor system wherein the lubricant is mixed with refrigerant during some portion of operation, and must later be separated from same. [0033] Finally, although the preferred embodiment of the present invention shows heat applied to the mixture within reclaim vaporizer 34 being supplied from hot gas discharged from compressor 12, the system of the present invention whereby heat exchange within vaporizer 34 is controlled to provide desired lubricant viscosity could be accomplished utilizing other sources of heat as well, and this is well within the broad scope of the present invention. [0034] An illustrative example of operation of the invention is provided herein. Assume a system as shown in Figure 1 is operating with valve 48 fully open. Mixture from evaporator 16 to reclaim vaporizer 34 is at a maximum flow rate. At this operation, control unit 50 has been programmed to maintain a difference (AT) between Tonj and Tref at between about a low value of X AND a high value of Y. Assume the temperature difference AT drops to a level which is less than X. At this point, control unit 50 would partially close valve 48 to slow the flow of mixture to reclaim vaporizer 34. This results in greater heating of the mixture and a higher Ton 1 , which also leads to an increase in AT. [0035] Assume that AT now exceeds the value Y. At this point, control unit 50 will open valve 48 further to increase flow of mixture to reclaim vaporizer 34. In this way, flow rate to reclaim vaporizer 34 is optimized to maximize oil 7 WO 2006/088459 PCT/US2005/005092 reclaim volume while maintaining the desired AT and, accordingly, a desired oil viscosity. [0036] Assume next that after the first partial closing of valve 48, the AT value remains less than X. Valve 48 is therefore closed further by control unit 50 to attempt to raise AT to the desired value. Control unit 50 continues to close valve 48 until valve 48 reaches a maximum closed setting wherein a minimum flow is fed to reclaim vaporizer 34. If at this point, AT is still too low, supplemental heater 46 can be activated to provide more heat and raise AT to the desired range. [0037] It should be appreciated that a control system has been provided according to the invention which advantageously provides control of oil viscosity in reclaimed oil whereby the viscosity can be maintained at desired levels, for example to ensure good lubrication and sealing at expected operating conditions of the compressor. [0038] It is to be understood that the invention is not limited to the illustrations described and shown herein, which are deemed to be merely illustrative of the best modes of carrying out the invention, and which are susceptible of modification of form, size, arrangement of parts and details of operation. The invention rather is intended to encompass all such modifications which are within its spirit and scope as defined by the claims. 8

Claims

1. A compressor system with controlled lubricant reclaim, comprising: a compressor circuit comprising a compressor, a condenser, and an evaporator connected by refrigerant flow line; a lubricant circuit for circulating lubricant to the compressor; a reclaim vaporizer adapted to heat a refrigerant lubricant mixture from the evaporator whereby the mixture is heated and lubricant and refrigerant are separated to provide reclaimed lubricant to the lubricant circuit and reclaimed refrigerant to the compressor circuit; and a control unit adapted to control flow of the mixture from the evaporator to the reclaini vaporizer based upon temperature of the mixture from the evaporator and temperature of reclaimed lubricant leaving the reclaim vaporizer.

2. The system of claim 1, wherein the control unit comprises a valve positioned along a discharge line for conveying the mixture from the evaporator to the reclaim vaporizer.

3. The system of claim 2, wherein the control unit is adapted to operate the valve to control flow rate of the mixture to the reclaim vaporizer so as to maintain a temperature difference between the reclaimed lubricant and the mixture within a preselected range..

4. The system of claim 1, wherein the control unit is adapted to control flow rate of the mixture to the reclaim vaporizer so as to maintain a temperature difference between 9 WO 2006/088459 PCT/US2005/005092 the reclaimed lubricant and the mixture within a preselected range.

5. The system of claim 1, wherein the reclaim vaporizer is communicated with discharge gas from the compressor to heat the mixture.

6. The system of claim 5, further comprising a supplemental heater for providing additional heat to the mixture in the reclaim vaporizer.

7. The system of claim 1, wherein the compressor is a screw compressor.

8. A method for controlling reclaim of lubricant in a compressor system, comprising the steps of: operating a compressor circuit comprising a compressor, a condenser and an evaporator and a lubricant circuit for circulating lubricant to the compressor so as to provide a refrigerant-lubricant mixture leaving the evaporator; exposing the mixture to heat in a reclaim vaporizer so as to provide reclaimed lubricant to the lubricant circuit and reclaimed refrigerant to the compressor circuit; and controlling flow rate of the mixture to the reclaim vaporizer based upon temperature of the mixture leaving the evaporator and temperature of the reclaimed lubricant leaving the reclaim vaporizer.

9. The method of claim 8, wherein the controlling step comprises sensing the temperature of the mixture and the reclaimed lubricant, and controlling flow of the mixture to the reclaim vaporizer to maintain a temperature difference between reclaimed lubricant temperature and mixture temperature within a preselected range. 10 11

10. A method for controlling reclaim of lubricant in a compressor system, comprising the steps of: operating a compressor circuit comprising a compressor, a condenser and an evaporator and a lubricant circuit for 5 circulating lubricant to the compressor so as to provide a refrigerant-lubricant mixture leaving the evaporator; exposing the mixture to heat in a reclaim vaporizer so as to provide reclaimed lubricant to the lubricant circuit and reclaimed refrigerant to the compressor circuit; 10 sensing a parameter indicative of reclaimed lubricant viscosity; and controlling rate of exposure of the mixture to heat based upon the parameter. 15

11. The method of claim 10, wherein the controlling step comprises at least one of controlling flow of mixture to the reclaim vaporizer, controlling amount of heat applied to the mixture and combinations thereof, so as to maintain reclaimed lubricant viscosity within a preselected range. 20

12. The method of claim 11, wherein the sensing step comprises sensing temperature of the mixture leaving the evaporator and temperature of the reclaimed lubricant leaving the reclaim vaporizer. 25

13. The method of claim 10, wherein the sensing step comprises sensing temperature of the mixture leaving the evaporator and temperature of the reclaimed lubricant leaving the reclaim vaporizer. 30

14. The method of claim 10, wherein the controlling comprises is responsive to a temperature difference between reclaimed lubricant temperature and mixture temperature. 35

15. The method of claim 10, wherein the controlling comprises controlling flow of the mixture to the reclaim vaporizer to maintain a temperature difference between reclaimed lubricant temperature and mixture temperature within a preselected range. 12

16. The system of claim 6 wherein the control unit is adapted to control the supplemental heater in combination with said control of said flow. 5

17. The system of claim 6 wherein the control unit is adapted to control the supplemental heater in combination with said control of said flow so as to maintain a temperature difference between the reclaimed lubricant and the mixture within a preselected range. 10 CARRIER CORPORATION WATERMARK PATENT & TRADE MARK ATTORNEYS 15 P29135AUOO