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CHAPTER 3: HEA T PUMP SIMULA TIONMoDEL _.---------- P_suc P dis I T_ev Tgc_o I mass Q (kW) 45 P (kW) 17.4 17.4 17.4 11.7 11.7 14.7 17.9 17.9 17.9 17.9 19.5 19.5 COP 3.245 2.863 2.322 6.387 5.525 3.725 4.058 3.705 3.256 2.624 3.68 3.352 60 Qh eta_c ! 56.47 0.659 49.81 0.6559 40.39 0.5744 74.73 0.5752 64.65 0.5766 54.76 0.6162 72.63 0.6666 66.33 0.6719 58.28 0.6695 46.97 0.5847 71.76 0.6493 65.37 0.6497 (kPa) 3969 3969 3969 I 4501 (kPa) (K) 12000 278 12000 278 12000 278 7500 283 7500 i 283 9000 283 12000 283 12000 283 12000 283 12000 283 13000 283 13000 283 ut (K) 298 08 313 288 298 308 288 298 308 313 288 298 flow i i 4501 4501 4501 4501 4501 4501 4501 4501 i A Techno-Economical Analysis of a CO2 Heat Pump. School of Mechanical Engineering, North-West University I 0.2324 0.2313 38.4 0.2026 30.4 0.3238 68 0.3246 57.9 0.3141 45.7 0.2814 60.7 0.2837 54.3 0.2826 46.3 0.2468 36.5 0.2729 59.1 0.2731 52.7PDF 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
Heat Pumps CO2 ORC Heat Pump System Platform More Info
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