2019
DOI: 10.1002/9783527809479
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Chemical Thermodynamics for Process Simulation

Abstract: 2 2.1 2.2 2.3 2.4 2.4.1 2.4.2 2.4.3 2.4.4 2.5 2.5.1 2.5.2 2.5.3 2.5.4

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Cited by 170 publications
(312 citation statements)
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“…Notice that Equation (1) does not describe solid-solid transitions, which are not present in the systems herein studied. The influence of the heat capacity term tends to be very small in most systems [44,45], in particular if the temperature is not too far from the melting temperature of the pure compound. Moreover, the D m Cp value is not available for most compounds used in this work due to a variety of reasons, one of which is thermal decomposition, as is the case of choline chloride.…”
Section: Thermodynamic Frameworkmentioning
confidence: 99%
“…Notice that Equation (1) does not describe solid-solid transitions, which are not present in the systems herein studied. The influence of the heat capacity term tends to be very small in most systems [44,45], in particular if the temperature is not too far from the melting temperature of the pure compound. Moreover, the D m Cp value is not available for most compounds used in this work due to a variety of reasons, one of which is thermal decomposition, as is the case of choline chloride.…”
Section: Thermodynamic Frameworkmentioning
confidence: 99%
“…Water activity coefficients of aqueous [DBNH][OAc] solutions were calculated using Equations (1) and (2). Gmehling et al [21] derived Equation (1) for the solubility of an organic solute in a solvent starting from the isofugacity condition. It can be used to estimate the activity coefficient of a sub-cooled liquid solvent as a function of the enthalpy of fusion, heat capacity difference between liquid and solid phase, and melting point of the solvent.…”
Section: Water Activity Coefficientmentioning
confidence: 99%
“…The viscosity and thermal conductivity of n-butanol in liquid and vapor phases were modeled using the following [58]:…”
Section: Butanol As An Alternative Fuelmentioning
confidence: 99%