1999
DOI: 10.1006/jcht.1998.0451
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Thermodynamic properties of the methylpyridines. Part 2. Vapor pressures, heat capacities, critical properties, derived thermodynamic functions between the temperatures 250 K and 560 K, and equilibrium isomer distributions for all temperatures ≥250 K

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Cited by 26 publications
(9 citation statements)
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“…There is an extensive literature 112 for the methyl derivatives of pyridine primarily from calorimetric measurements of the heat of combustion; these have been reanalyzed by Chirico et al 113 who concluded that the work by Andon et al 96 was most likely correct except for their value for 3-methylpyridine, Table 11. This work concurs with that assessment and also that the more recent determination for the 3-methyl by Gerasimov et al 114 of 103.6 ± 1.3 kJ mol −1 is much nearer the mark.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
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“…There is an extensive literature 112 for the methyl derivatives of pyridine primarily from calorimetric measurements of the heat of combustion; these have been reanalyzed by Chirico et al 113 who concluded that the work by Andon et al 96 was most likely correct except for their value for 3-methylpyridine, Table 11. This work concurs with that assessment and also that the more recent determination for the 3-methyl by Gerasimov et al 114 of 103.6 ± 1.3 kJ mol −1 is much nearer the mark.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…There is an extensive literature for the methyl derivatives of pyridine primarily from calorimetric measurements of the heat of combustion; these have been reanalyzed by Chirico et al . who concluded that the work by Andon et al was most likely correct except for their value for 3-methylpyridine, Table .…”
Section: Beyond Atctmentioning
confidence: 99%
“…Calculation of C sat,m values from the values listed in Table has been described. , Reliable vapor pressures and densities for the liquid phase are required for the calculation of C sat,m values. The Wagner equation (eq 3) was used with the parameters listed in Table for the vapor pressures, and densities were calculated with eq 4, also with the parameters in Table .…”
Section: Resultsmentioning
confidence: 99%
“…Calculation of C sat,m values from the values listed in Table has been described. , Reliable vapor pressures and densities for the liquid phase are required for the calculation of C sat,m values. The Wagner equation (equation 5) was used with the parameters listed in Table for the vapor pressures, and densities were calculated with eq 6, also with the parameters in Table .…”
Section: Resultsmentioning
confidence: 99%