2019
DOI: 10.1021/acs.jced.9b00578
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Combined Thermogravimetric Determination of Activity Coefficients and Binary Diffusion Coefficients—A New Approach Applied to Ferrocene/n-Tetracosane Mixtures

Abstract: The use of isothermal thermogravimetry is investigated for combined measurements of activity coefficients and diffusion coefficients in binary mixtures, where the vapor pressure is dominated by one compound. The coupling of evaporation with gas phase and condensed phase diffusion leads to an unsteady mass loss, which depends on the activity coefficient and both, gas phase and condensed phase, diffusion coefficients, as is explained. This can be used to measure two of these properties, if the remaining paramete… Show more

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Cited by 2 publications
(4 citation statements)
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“…x T = 7.4 × 10 −5 to 8.2 × 10 −4 from previously measured vapor pressure data by the group. [5] Given this, reasonable Arrhenius plots were derived using the integral method for the unimolecular dissociation reaction of ferrocene (see Section 2.6). Since unimolecular gas-phase dissociation reactions of metal-organic precursors often follow firstorder kinetics, which was also determined here experimentally, the rate constant was approximated using the Arrhenius law shown in Equation ( 6):…”
Section: Methodsmentioning
confidence: 99%
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“…x T = 7.4 × 10 −5 to 8.2 × 10 −4 from previously measured vapor pressure data by the group. [5] Given this, reasonable Arrhenius plots were derived using the integral method for the unimolecular dissociation reaction of ferrocene (see Section 2.6). Since unimolecular gas-phase dissociation reactions of metal-organic precursors often follow firstorder kinetics, which was also determined here experimentally, the rate constant was approximated using the Arrhenius law shown in Equation ( 6):…”
Section: Methodsmentioning
confidence: 99%
“…Three separate experiments operating at an evaporator pressure of 1500 mbar and sublimation temperatures of 323/333/353 K were conducted. Assuming thermal equilibrium, the precursor mole fractions at the reactor inlet are calculated from the vapor pressure data [ 5 ] to be between x Fe(C5H5)2 = 7.4 × 10 −5 – 8.2 × 10 −4 . After sublimation, the mixture is expanded through a 100 µm pinhole into a resistively heated silicon‐carbide (SiC) [ 102 ] flow reactor with an inner diameter of 1.0 mm and a heated length of 10 mm.…”
Section: Methodsmentioning
confidence: 99%
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