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Pressure-temperature relations

Let the pure phases of components A and B be denoted by single and double primes respectively. The solution phase will be denoted by symbols without a prime. The condition of equilibrium for component A is,  [Pg.217]

Multiplying the first equation by x and the second by (1— ) and adding, we obtain by use of equation (7 4) [Pg.217]

B) be simultaneously precipitated. In these proportions the composition of the solution remains unchanged. The heat absorbed in this process is may be denoted AJ . The [Pg.218]

As in the case of the Clausius-Glapeyron equation, it is usuaUy a good approximation to put AFs RTjp equivalent to neglecting all terms except in (7 9) and also assuming the vapour to be perfect. Hence [Pg.218]

It is to be noted that AH includes both the enthalpy of vaporization of water from the given solution and the enthalpy of precipitation of r moles of the solute. [Pg.218]


Fig. 13.— Pressure-Temperature Relations Fig. 14.—-Vapour Pressures of Phos-of Mixtures of Phosphine and Hydrogen phonium Chloride. Fig. 13.— Pressure-Temperature Relations Fig. 14.—-Vapour Pressures of Phos-of Mixtures of Phosphine and Hydrogen phonium Chloride.
The heat of sublimation of violet phosphorus can be calculated from the pressure-temperature relations in a similar manner. In the first place, c is calculated by equation (2) (p. 36) between T1 = 343-5+273 and T2 = 589-5 +273 and is found to be 18-9. Since the TlnpjT graph is found to be rectilinear over this range of temperature it follows that Qsv does not vary much, and it was possible to write the linear equation... [Pg.37]

Wiener, H. (1948b). Vapour Pressure-Temperature Relations among the Branched Paraffin Hydrocarbons. J.Phys.Chem., 52, 425-430. [Pg.662]

The pressure-temperature relations for the CH4 s-H hydrates were measured under four-phase equilibrium condition. The s-H hydrate formation was observed in the CH4+CI-DMCH, CH4+MCH, CH4+c-Octane, CH4+c >l,2-DMCH, CH4+c/ -l,4-DMCH and CH4+MCP systems. The equilibrium pressure of each s-H system increases in that order at isothermal condition and it is lower than that of pure CH4 s-I hydrate. The 1,1-DMCH molecule has the best molecular-size to fit the E-cage cavity and constructs the CH4 s-H hydrate at the lowest pressure in the all LGS of present study. [Pg.369]

Pressure-Temperature Relations between Stable and Meta-stabie Forms.—Since the possibility of the existence of a substance in a metastable state must be recognised, it becomes of importance to consider what relationship exists between the vapour pressure of the stable and metastable forms. [Pg.39]

Pressure Temperature Diagram.— The consideration of the pressure-temperature relations of the two components, sodium sul-... [Pg.178]

Univariant Systems.—Equilibrium between liquid and vapour. Vaporisation curve. Upper limit of vaporisation curve. Theorems of van t Hoff and of Le Chatelier. The Clausius-Clapeyron equation. Presence of complex molecules. Equilibrium between solid and vapour. Sublimation curve. Equilibrium between solid and liquid. Curve of fusion. Equilibrium between solid, liquid, and vapour. The triple point. Complexity of the solid state. Theory of allotropy. Bivariant systems. Changes at the triple point. Polymorphism. Triple point Sj—Sg— V. Transition point. Transition curve. Enantiotropy and monotropy. Enantiotropy combined with monotropy. Suspended transformation. Metastable equilibria. Pressure-temperature relations between stable and metastable forms. Velocity of transformation of metastable systems. Metastability in metals produced by mechanical stress. Law of successive reactions. [Pg.335]

From an energy balance alone we can relate temperature to the Mach number for steady, adiabatic flow (isentropic or nonisentropic). By using the pressure-temperature relation for an isentropic change in an ideal gas, we can complete the mathematical description of steady, frictionless, adiabatic, perfpct-gas flow. The mass balance equation is used to solve for the cross-sectional area perpendicular to the flow. [Pg.322]

B. Pressure-Temperature Relations Between Stable and Metastable Phases... [Pg.36]

Uranium self-diffusion in UN has quite recently been measured by Reimann et al. (333) based on an assumed pressure-temperature relation for constant composition. The results obtained, however, would indicate that the composition of the sample was not constant during the measurement. They presumed from the pressure dependence of D that uranium diffusion in UN is based on the vacancy mechanism. [Pg.155]

Figure 8.13. Pressure and temperature in an autoclave (a) pressure-temperature relation for different fill ratios (in % of volume) of the autoclave in percent (drawn curve indicates the equilibrium relation of water) (b) process condition in a typical run during a hydrothermal process. Figure 8.13. Pressure and temperature in an autoclave (a) pressure-temperature relation for different fill ratios (in % of volume) of the autoclave in percent (drawn curve indicates the equilibrium relation of water) (b) process condition in a typical run during a hydrothermal process.
Fig. 8. Pressure-temperature relation for three reactor core compositions. Fig. 8. Pressure-temperature relation for three reactor core compositions.

See other pages where Pressure-temperature relations is mentioned: [Pg.1140]    [Pg.619]    [Pg.43]    [Pg.204]    [Pg.126]    [Pg.25]    [Pg.25]    [Pg.490]    [Pg.11]    [Pg.25]    [Pg.322]    [Pg.21]    [Pg.41]    [Pg.28]    [Pg.31]    [Pg.40]    [Pg.446]    [Pg.25]   


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