2015
DOI: 10.1021/je5010565
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Solid–Liquid Phase Equilibrium of Phosphoramidic acid, N,N′-1,2-Ethanediylbis-P,P,P′,P′-tetraphenyl Ester in Selected Solvents

Abstract: Phosphoramidic acid, N,N′-1,2-ethanediylbis-P,P,P′,P′-tetraphenyl ester (PAETE) was prepared and characterized by elemental analysis (EA), mass spectra (MS), infrared spectroscopy (IR), and nuclear magnetic resonance (NMR). The thermostability of PAETE was measured via thermogravimetric analysis (TGA). The melting temperature and the fusion enthalpy of PAETE were evaluated by differential scanning calorimeter (DSC). The solubilities of PAETE in ten selected solvents were obtained using a gravimetric method. Th… Show more

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Cited by 10 publications
(11 citation statements)
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“…Equation (7e) gives the death rate expression due to disintegration of droplets V. All the above expressions are required to be closed by appropriate disintegration and coalescence kernel functions, represented by r D and r C respectively. These are defined in accordance with the various coalescence [27][28][29][30] and disintegration [8,27,31] mechanisms proposed in the literature. Wang et al [32] compared various coalescence and breakage kernels.…”
Section: Population Balance Modelsmentioning
confidence: 81%
“…Equation (7e) gives the death rate expression due to disintegration of droplets V. All the above expressions are required to be closed by appropriate disintegration and coalescence kernel functions, represented by r D and r C respectively. These are defined in accordance with the various coalescence [27][28][29][30] and disintegration [8,27,31] mechanisms proposed in the literature. Wang et al [32] compared various coalescence and breakage kernels.…”
Section: Population Balance Modelsmentioning
confidence: 81%
“…Nevertheless, the correlation coefficient is between 0.9-0.93, which is considered to be reasonably acceptable in comparison with the model. [36,42] Figure 2b presents radial distributions of the axial component of time-averaged liquid velocity (calculated without being weighted…”
Section: Comparison Of Model Predictions With Experimental Resultsmentioning
confidence: 99%
“…Thus the classes must be defined a priori, and a large number of classes may be required. The classes of bubble diameters used in this work are based on the sensitive study of Chen et al, [ 1 ] as listed in Table 4. The bubble diameter of the gas inlet is set to 5.00 mm.…”
Section: Mathematical Modellingmentioning
confidence: 99%
“…Recently, computational fluid dynamics (CFD) have become an indispensable tool for analyzing bubble column flows, and the Euler‐Euler method, which treats both gas and liquid phases as continuous media, has been frequently employed among various simulations. [ 1–5 ]…”
Section: Introductionmentioning
confidence: 99%