Background of the Invention
This invention relates to a vapor cycle cooling system. various air cycle cooling systems using rotary vane compressor-expander apparatus are described in the patents to Edwards, U.S. Pat. No. 3,686,893; 3,913,351; 3,967,466 and 3,977,852. These systems provide a compressor and an expander within the rotor housing to provide cooling.
Various complex compression vapor cycle systems are described on pages 46-74 of "Refrigeration and Air Conditioning" by B. F. Raber et al., published by John Wiley and Sons, Inc., in February 1949. However, no practical complex cycle apparatus is described.
The patent to Weatherston, 3,808,835, describes a cooling system wherein refrigerant vaporized at an intermediate pressure is supplied to closed volume chambers of the compressor.
Brief Summary of the Invention
According to this invention a rotary vane compressor-expander normally used in an air cycle cooling system, as described in the patents to Edwards, is modified to provide a two-stage compressor for a two-phase vapor cycle cooling system. The vaporized refrigerant at an intermediate pressure is supplied to the two stage compressor at a position between the two stages of compression.
In the Drawing
FIG. 1 is a partially schematic diagram of a cooling system according to one embodiment of the invention.
FIG. 2 is a partially schematic diagram of an another embodiment of the invention.
Detailed Description of the Invention
Reference is now made to FIG. 1 of the drawing which shows a vapor-cycle cooling system 10 including a conventional compressor-expander rotary vane device 12, which has been modified to provide a two stage compressor. The rotary vane device 12 includes a rotor 14 within a chamber 15 in housing 16. The rotor has a plurality of radial slots 18 for receiving slidable vanes 20. Any of the prior art blade guide means, not shown, may be provided for the control of vane movement in the slots. The rotor is driven in the direction shown by arrows 22, through shaft 24 by a drive means 26, such as in electric motor or a drive belt driven by the motor of an automobile. As shown in FIG. 1 the rotor body 28 is positioned a greater distance from the chamber wall 30 on the low pressure side 32 of rotor 14 than on the high pressure side 34 of chamber 15. For example, assuming a 2.50 to 1 pressure ratio across each compressor, the spacing of the wall 30 from the rotor on side 32 would be approximately twice the spacing of the wall 30 from the rotor on side 34.
The working fluid used could be a hydrocarbon such as R-12, R-22, or R-114. The working fluid from evaporator 38 is supplied to inlet 40 of the first compressor stage 33 on side 32 of chamber 15; with the output of the first compressor stage being taken off at 42. The output from the first compressor stage is supplied to inlet 44 of the second compressor stage 35 with the output of the second stage being taken off at 46. The output of the second compressor stage is supplied to a condenser 48. The output of condenser 48 is supplied to an expansion valve 50 with the output of the valve 50 being supplied to a receiver 52 wherein the vapor phase coolant is collected and added to the coolant that is supplied to the input 44 of the second compressor stage. The liquid phase coolant from receiver 52 is supplied to a second expansion valve 54, with the output of the second expansion valve 54 being supplied to an evaporator 38.
In the operation of the device of FIG. 1, the output of the evaporator 38 is supplied to inlet 40 of the first compressor stage 33 with the output of the compressor stage being taken off at 42 and fed to the inlet 44 of the second compressor stage 35. Inlets 40 and 44 extend around the periphery of chamber 15 in the regions of normal expansion of the volume between adjacent vanes 20. The output of the second compressor stage 35 is supplied to condenser 48 wherein heat is removed in a conventional manner. The output of condenser is supplied to two stages of expansion in valves 50 and 54. Vapor produced in the first expansion is separated in receiver 52 and added to the flow between outlet 42 and inlet 44 wherein it provides a small amount of cooling for the flow between the compressor stages. After the liquid coolant from receiver 52 undergoes the second expansion it is supplied to evaporator 38 where it absorbs heat in a conventional manner.
A device for providing a higher coefficient of performance than the device of FIG. 1 is shown in FIG. 2. In the device of FIG. 2 the rotary vane device 12 operates in the same manner as in FIG. 1 but the output of the condenser 48 is divided into two flow paths 60 and 62. The flow in path 60 passes through heat exchanger 64 to an expansion valve 54'. The flow in path 62 passes through an expansion valve 66 which lowers the temperature of the coolant after which the coolant in flow path 62 is supplied to heat exchanger 64 wherein it removes heat from the flow in flow path 60. The lower temperature coolant flowing through expansion valve 54' provides increased cooling in evaporator 38. The device of FIG. 2 otherwise operates in a similar manner to the device of FIG. 1.
There is thus provided an apparatus which makes use of a rotary vane device as a two stage compressor in a two phase cooling system, which provides a higher coefficient of performance than prior art devices.