PDF Publication Title:
Text from PDF Page: 175
Table 1. Results of chemical analyses for some selected samples. Sample Co-LSX Co(flo)-LSX Co(flo)-MCM-41 Co C F wt% wt% wt% 18.0 - - 16.0 13.51 2.04 5.9 11.97 1.88 Table 2. Experimental O2 capacities (at 25 C, 1 atm) for various O2-binding materials compared to the theoretical capacities for 1:1 and 1:2 (O2:Co2+) adducts. Material Co(salen) Co(fluomine) Co(fluomine)-LSX Co(fluomine)-MCM-41 Co(fluomine)-IXR Experimental O2 capacity mmol/g 1.06 1.13 0.123 0.107 0.03 Theoretical 1:1 adduct mmol/g 3.1 2.78 0.57 0.49 1.23 Theoretical 1:2 adduct mmol/g 1.55 1.39 0.29 0.25 0.616 NOTE: The experimental capacity is that measured at 25 C and 1 atm, the Co(fluomine)-LSX result is corrected to account for the natural O2 capacity for Co-LSX. The theoretical amounts for the Co(fluomine)-LSX assume two Co(fluomine) molecules per zeolite cavity. The Co(fluomine)-MCM-41 theoretical amounts assume 3.7 Co(fluomine) molecules per unit cell. The Co(fluomine)-IXR theoretical amounts assume 100% Co2+ ion exchange and subsequent conversion to Co(fluomine). The cation exchange capacity for the LSX zeolite is 7.4 meq/g; the MCM-41 is 1.48 meq/g; and the ion-exchage resin is 4.7 meq/g. 175PDF Image | PSA USING SUPERIOR ADSORBENTS
PDF Search Title:
PSA USING SUPERIOR ADSORBENTSOriginal File Name Searched:
789503.pdfDIY PDF Search: Google It | Yahoo | Bing
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
| CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com | RSS | AMP |