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- I . 8 0 Polarity 0 Standard. after 20 40 60 80 100 120 140 Currentdensity, m ~ l c m ~ 1- Y285-64C W285-9039 U285-87 W285-89 W285-99 (7mii) W285-99 (4mi1) MT306-34 1 Type ( Sourcc 1 Figure 24 - Effed of complete polarity reversal on performance. BismuthCatalyst:ML-21membrane: stateofcharge. 50per- cent: temperature, 65 OC; mixed r-ctants: bismuth salt i n each reactant 70I f u For (a) Coulombicefficiency. 60 s s 20 40 60 80 100 1M 140 160 Current density, m ~ l c m ~ (bl Energyefficiency. Figure 25 - Effect of current densi2on working cell efficiency for developn~entaml embranes. current cycles: temperature. 65 C: mixed reactants. CPS-1 TABLE V. - EFFECT OF TEMPERATURE ON SELECTIVITY OF MEMBRANES FOR ELEVATED-TEMPERATURE OPERATION WITH MIXED REACTANTS 0 w7U-39 0 W285-99CI mill v W285-99 (4 mill 0 ML-2l D 1155-2l4-45 Cation Temperature, *C 2210 --- 35 Asahi 60 RA I 770 180 200 Constant-PDF Image | NASA Redox Storage System Development Project
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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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