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CHAPTER 3: PU1\1P SIJ:vfULATION MODEL 67 o 2000 4000 6000 6000 10000 12000 Figure 3.11: Coefficients aO against discharge pressure. -+--a1 -Poly. (al) 14000 Figure 3.10: Coefficients a1 against discharge pressure. As in the first few plots, a polynomial equation is fitted through the different plots with R2-equation showing the accuracy of the plot. The polynomial equation resulted in 3rd order polynomial equations taking the discharge pressure into consideration as well. The 3rd order polynomials taking the discharge pressure into account are given below: y:::::: -2.1646xlO-9 x2 +4.2438xlO-5 x R2 9.8358xlO-1 A Techno-Economical Analysis of a CO2 Heat Pump. School ofMechaoical Engineering, North-West University 2.0742xlO-1 [3.14] •PDF Image | CO2 HEAT PUMP Analysis
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CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info
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