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Membrane 0 W285-9039 o W285-99 17mil) . 2 )- I ( ) A J o 2 4 5 8 JO12x103 Diffusionrate. pgFelhcn,M Figure a. - Experimental c;orrelat!on of selectivity and resistivity for develop- mental membranes. ORiGIP!.RL F-. . OF POOR G,-,,!-! ,' TABLE VI. - EFFECT OF CURRENT PENSITY ON REDOX CELL EFFICILYCY [lonics W285-09 (7 mi1) membrane; temperature, - emb bran;^^^^ - - W285-9039 1155-213-45 Ionics 210 200C 1 3700 I 1 I TABLE V I I . - REDOX CELL PCDFORMANCE FOR VARIOUS MEMBRANES AT THEIR RESPECTIVE PPTIMUM CURRENT DENSITIES 1155-214-45 W285-99 (4 mil) Ionics 2900 93 3100 lcpSl 1Ionics 1 - -- :: -- -2 ~ 65' C, , . ~ ~ rtedactants.] ~ ~ ~ y ~ !&~I T + 114.5-cm2 cell; temperature, 65' C; mixed reactants.] [ current, re sistiv'ty, ef ficiency, ef ficiency, g S Fe 1e e/ ch t r i vc r i ' . 1.19 .53 .59 : 1:: i 1 TABLEVIII. -EFFECTOFCURRFNT DENSITY ON REACTANT UTILIZATION FOR CONSTANT-CURRENT CYCLES BETWEEN CUTOFF VOLTAGES OF 1.20 V and C.76 V [Cell resistivity, 0.8 ohm-cm2; reactant flow rate, 1.5 times stoichiometrir. 1 utilization, -1 1 uPDF 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
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