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CHAPTER 2: LITERA TURE STUDY 20 Figure 2.6: Enthalpy change of CO2 in the gas cooling process. (Kim et ai, 2003). 0 J~ ~100 0 >. 15l a. .c; oJ:::: +' t: W -200 --4MPa ---SMPa -0.6 -0.8 j--( ~ ----- -1 ,.x; -0 ) J ,.x; \......t -1.2 >. a. 0 ,..., -1.4 ...... t UJ --4MPa --- 8MPa ~10MPi3 -- 12MPa ~~14MPa 80 100 '120 -300 --iOMPa. --- 12MP:a. _...... 14MPa. -4001....----1._-"-_-'--_'--'"_~_J..__.!.__'l___'__ _"__ _ '_ _ _ '_ _ _ .J -20 a 20 40 60 so 100 120 Figure 2.7: Entropy change of CO2 in the gas cooling process. (Kim et ai, 2003). ~O.4 ~i.6 -1.8 o 20 40 60 Figures 2.6 and 2.7 show how the enthalpy and entropy of CO2 changes in the gas cooling process at constant pressures. The enthalpy and entropy decreases with temperature in the super-critical region. More distinct changes in enthalpy and A Techno-Economical Analysis of a CO2 Heat Pump. School ofMechanical Engineering, North-West UniversityPDF 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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