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Figure 11. COP using different compressor efficiencies (top), pressure drops (middle) and ejector efficiencies (bottom). The green circles indicate where R744 and R410A curves cross. Taππble 3. COP for different heating ratios ππhππππππ and ejector efficiencies scenarios. π‘π‘π‘π‘π‘π‘π‘π‘ COP [-] (Gain in COP by inclusion of an ejector [%]) [-] 0.0 1.0 5.0 R744 R410A R744 ABC + R744 ABC + R744 ABC + ABC ABC ejector 17 % ejector 25 % ejector 34 % R410A ABC + ejector 17 % 4.44 (1.2 %) 5.12 (0.6 %) 5.42 (1.7 %) R410A ABC + ejector 34 % 4.51 (2.7 %) 5.15 (1.2 %) 5.49 (2.9 %) 4.67 4.39 4.74 5.09 4.10 5.33 4.77 (2.2 %) 4.91 (3.6 %) 4.37 (6.4 %) 4.82 (3.0 %) 4.95 (4.7 %) 4.49 (8.8 %) 4.87 (4.4 %) 5.10 (7.4 %) 4.56 (11.0 %) 12PDF Image | CO2 Heat Pump Performance
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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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