1966
DOI: 10.1021/j100879a050
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Thermodynamic Properties of Gases in Propellants and Oxidizers. I. Solubilities of He, N2, O2, Ar, and N2O3 in Liquid N2O4

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Cited by 17 publications
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“…The solubilities of C02 and SF6 in N204 are summarized in Table IV and represented in Figure 3. The corresponding equations for AG°are as follows: AG°(C02 in N204) = -2,828 + 17.33 T AGa(SFe in N204) = -1,748 + 15.44 T The values of AH0 are strongly negative in both systems because C02 and SF6 do not break up the N02-N02 bond in N204 as He, Ar, N2, and 02 in N204 (1). The solubility of C02 in N204 is close to the ideal solubility at 1 atm computed from X(C02) = l//°, where/0 is the fugacity of pure liquid C02 at the temperature of interest, and X is the mole fraction.…”
Section: Resultsmentioning
confidence: 99%
“…The solubilities of C02 and SF6 in N204 are summarized in Table IV and represented in Figure 3. The corresponding equations for AG°are as follows: AG°(C02 in N204) = -2,828 + 17.33 T AGa(SFe in N204) = -1,748 + 15.44 T The values of AH0 are strongly negative in both systems because C02 and SF6 do not break up the N02-N02 bond in N204 as He, Ar, N2, and 02 in N204 (1). The solubility of C02 in N204 is close to the ideal solubility at 1 atm computed from X(C02) = l//°, where/0 is the fugacity of pure liquid C02 at the temperature of interest, and X is the mole fraction.…”
Section: Resultsmentioning
confidence: 99%