<p>Due to increasing environmental concerns and stringent
regulations, the Heating, Ventilation, Air Conditioning, and Refrigeration
(HVAC&R) industry is working to develop technologies that utilize
low-global warming potential (GWP) refrigerants and remain within competitive
coefficient of performance (COP) values and capacities of current hydrofluorocarbon
(HFC) systems. Carbon Dioxide (CO<sub>2</sub>) has been investigated
extensively over the past 25 years as a potential substitute for HFCs in refrigeration
applications in mild ambient climates. Through efforts to increase the efficiency
of CO<sub>2</sub> systems, researchers and industry have identified cycle
modifications that are particularly beneficial in transcritical CO<sub>2</sub>
cycle applications, such as expansion work recovery and economization. Yet,
systematic experimental comparisons between these cycle enhancements are still
lacking in the open literature. This thesis presents the design, assembly, and
operation of a multi-stage, two-evaporator transcritical CO<sub>2</sub> cycle
with a combined capacity between the two independently-controlled evaporators
of approximately 8 kW. The cycle utilizes three stages of compression, intercooling
between the second and third stages, and flash tank economization at the medium-temperature
evaporator. Furthermore, the test stand was designed to enable on-line
transition between three methods of expansion without the need to stop the
compressors. In particular, expansion through an electronic expansion valve (EXV),
ejector, and through an ejector with a pump used to modulate the ejector inlet
state are investigated. The purpose of this experimental work is to provide a
comprehensive comparison between these cycle architectures and methods of
expansion work recovery as well as to assess both the pump and variable motive
nozzle diameter as means of ejector control and system performance enhancement.
Experimental testing assessed the performance of cycles utilizing
economization, an ejector, and an ejector with a pump over four ambient
conditions from 14 °C to 28 °C.
The evaporator source temperatures were fixed to simulate refrigeration and
freezing conditions. The pump controlled the ejector effectively and increased
the ejector efficiency by up to 41%, despite decreasing the cycle COP. COP
improvements of 6% and 5% were achieved with the open economization and ejector
cycles, respectively.</p>
<p>In addition to the experimental aspects, a numerical
ejector design tool that can be applied to a vapor compression cycle was
developed. The model solves each subcomponent of the ejector intensively, and
receives inputs of mass flow rates, geometric angles, and ratios to output physical
dimensions of an ejector. The design tool agreed with experimental dimensions
with a mean absolute error (MAE) of 3% to 4%.</p>
<p>A second numerical aspect of this thesis consists of a
dynamic model of the transcritical CO<sub>2</sub> vapor compression cycle test
stand used for experimental testing. The dynamic model can be used to predict
both steady state performance and dynamic performance of the system, and
employs component models for the heat exchangers, compressors, and expansion
valves utilized in the experimental setup. Steady state validation resulted in
maximum MAE of 18.7% and 11.9% for cooling capacity and power consumption,
respectively, and dynamic validation resulted in similar thermal time scales
between experimental data and the simulation. An evaporator pull down and an
evaporator excitation simulation were successfully implemented to validate the
ability of the model to develop control schemes.</p>
<p>Experimental future work consists of both cycle modification
recommendations and control method implementation. Ejector design future work
is the implementation of higher-fidelity sub-component models, and future work
for the dynamic model is the thorough characterization of mass transfer and
development of models of additional cycle architectures.</p>