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CHAPTER 4: COMP ARlSONBETWEENR-22AND CO2 SYSTEM 113 900 800 700 ~ 600 .r: :s: .:.: ;:: 500 Cl lii ;; 400 > 0'" 300 200 100 Figure 4.21: Summary of yearly energy consumption for the R-22 the system. 0 0 30 60 90 120 150 180 210 240 270 300 330 360 390 Day Figure 4.22: Summary of yearly energy consum ption for the ILH the system. 1400~--~----,-------~----.-------~~--,---~----c---~--~----, 800 > E' Q) c: Q) 600 ia' o 400 -.,''',.,.,''''-'''----+--'''''''''''''''''-,---'------i--"-,.,'-''-''''.+,--".,,--i-··,"""'"·,-,,,·,,-"----r'-·----'-"""'-,,-<----I 200 ,,-'''-,-,----4,.,.-,,--''''''''',.,.,,--,,-,--....,-.,----'-'''',.,..--;---·"''''''''''1 '''''---,'''''-,,..,,·+'''',,·-''''---,,-''''--,-,,---1 o 30 60 90 120 150 180 210 240 270 300 330 360 390 Day A Techno-Economical Analysis of a COl Heat Pump. School of Mechanical 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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