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65 60 55 50 45 40 35 30 25 20 0 9 8 7 6 5 4 T_top T1 T2 T3 T4 1800 3600 5400 7200 9000 10800 12600 14400 T_rad_supply water gas T_rad_return Flow heat_cap transient tank behavior under frosting/defrosting conditions with 3,4kW radiator load at -2°C Tamb- 2008-04-17 time [s] Figure 29. Tank temperature distributions during defrosting period (electric heater at off-mode, with radiator load) 70 60 50 40 30 20 10 8 water gas cooler in Tank charging at +0 degreeC Tamb with no radiator load *- 2008-04-07 01 -10 0 0 1800 3600 5400 7200 9000 10800 12600 14400 time [s] Figure 30. Tank temperature distributions during defrosting period (electric heater at off-mode, no radiator load) 3 T5 T6 0 2 1 cooler in water gas cooler 7 out T1 6 T2 T3 T4 T5 compr. power COP Flow normalized [x/0,263m3/h] *radiator pump was working 5 4 3 2 temperature [°C] Temperature [°C] normalized flow [-]; power [kW]; COP [-] heating capacity [kW], Flow [m3/h] 37PDF Image | CO2 heat pumps for the Swedish market
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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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