Background - The very impressive Athens based R&D company, Sunpower, Inc, was formed by William Beale more than thirty years ago, mainly based on his invention of the free-piston Stirling engine. The free-piston configuration enabled Sunpower over the years to develop an internationally recognised expertise in linear motors and generators, and one of the byproducts of this development is the oil-free linear compressor for refrigeration applications.
The following drawing is reproduced from a paper by Sunpower (refer for example to the various technical papers on linear compressors which can be downloaded from Sunpower's website), and illustrates the significant difference between a regular mechanical slider-crank compressor mechanism and the linear compressor:

Some of the major advantages of the linear compressor are:
Sunpower exhibited the first commercial refrigerator using the linear compressor at the Sustainability Fair, which took place in the Athens Fairgrounds on October 14, 2001 (see picture). This is an extremely quiet and very impressive machine, and is manufactured by LG Electronics in Korea.
Problem
4.7 - We wish
to do a preliminary thermodynamic evaluation of a refrigeration
system designed for home usage which will use the linear compressor
with refrigerant R134a. Consider the following system flow diagram
(Note: the picture of
the Sunpower linear compressor was taken from Sunpower's website
with permission, however all other values shown in this diagram
are pure speculation on the part of your instructor for purposes
of this exercise):
Notice that no mass flow rate has been provided, thus all energy solutions should be specific quantities [kJ/kg]. Plot the four processes on the P-h diagram provided below and use the R134a refrigerant property tables in order to determine the following:

Internal
Heat Exchanger Addition - On a previous tour of Sunpower (October 2005) we were
told by the engineer in charge of linear compressor development
(Robi Unger) that it is common practice in the refrigeration industry
to use an internal heat exchanger to subcool the refrigeramt at
the outlet of the condensor by means of that exiting the evaporator
and thus obtain a much improved performance. Using that information
we have constructed a new system flow diagram as follows:
Notice that we have included an internal heat exchanger that heats the refrigerant exiting the evaporator (as a saturated vapor at 140kPa) to 20°C. We have chosen a state numbering system (1x, 2x, and so on) so as to allow the new system to be plotted on the same P-h diagram as Problem 1, and thus to be able to qualitatively compare the increase and improvement of performance provided by adding the internal heat exchanger. In order to determine the new value of enthalpy at state 3x we consider the heat transferred in the heat exchanger as in the following diagram:
Notice again that no mass flow rate has been provided, thus all energy solutions should be specific quantities [kJ/kg]. Show the additional processes superposed on the previous P-h diagram and use the R134a refrigerant property tables in order to determine the following:
Finally, comparing the two systems compare their respective performance and discuss the results.
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Engineering Thermodynamics by Israel Urieli is licensed under a
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Alike 3.0 United States License