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Vapour Antoine equation

The jacket steam pressure, Pj, is itself a function of the jacket steam temperature, Tj, as listed in steam tables or as correlated by the Antoine equation for vapour pressure, where... [Pg.137]

As boiling proceeds, the loss of the lightest organic vapours will cause the boiling point to increase with time. The vapour pressures Pj and P of the pure components can be calculated using the Antoine equation... [Pg.218]

The vapour pressures of the pure liquids can be calculated from the Antoine equation (see Chapter 8) ... [Pg.147]

The equation presented here, due to Haggenmacher (1946), is derived from the Antoine vapour pressure equation (see Section 8.11). [Pg.328]

At 200°C, the vapour pressure must first be estimated, from the Antoine equation ... [Pg.330]

Several equations have been developed to express vapour pressure as a function of temperature. One of the most commonly used is the three-term Antoine equation, Antoine (1888) ... [Pg.331]

The saturation vapour pressures are calculated as a function of temperature using the Antoine equation, equation 11.6, and the constants given in Example 11.3, and then, from Raoult s Law, Equation 11.1, the actual vapour pressures are given by ... [Pg.550]

The Antoine equation (16a) is normally used for a vapour-liquid mixture, whereas eq. (16b) is normally... [Pg.4]

Of course, the vapour pressure is very temperature dependent, and reaches P° = 101.325 kPa at the normal boiling point, Tb. The isochoric thermal pressure coefficient, dp/dT)v = otp/KT, can be obtained from the two quantities on the right hand side listed in Table 3.1. Except at T it does not equal the coefficient along the saturation line, (dp/dT)a, which is the normal vapour pressure curve. The latter temperature dependence is often described by means of the Antoine equation ... [Pg.136]

Mujtaba and Macchietto (1988) and Mujtaba (1989) used two typical binary mixtures and a variety of separation specifications to demonstrate how optimal recycle policies can be obtained and to assess the validity of the degree of difficulty measure. The mixtures were 1) Benzene-Toluene 2) Butane-Pentane. For simplicity ideal equilibrium and Antoine s vapour pressure equations were used. The light component was always the first one. [Pg.236]

From the published literature [89,744,860,1514,1591] assembled by Stull [1971], the vapour pressure data of phosgene have been processed [1541] in the form of the Antoine equation. Equation (6.3) ... [Pg.277]

The parameter is a general function of the acentric factor ca, while k is a parameter to be found by regression. The evaluation of accuracy showed an error in correlating the vapour pressure under 1%, typically between 0.2 and 0.3%. The accuracy of PRSV is by an order of magnitude better as PR EOS and the same as Antoine equation. SRK2 and PRSV are of comparable accuracy. [Pg.169]

The plots indicate that the non-ideality is significant at higher concentrations. Consequently, liquid activity coefficients should be used. Because NHj is subcritical, there is a choice between symmetric and asymmetric conventions. In the first case, Antoine equation is necessary for both components. In the second case, Henry constant for ammonia-water pair is required, but this may be obtained from the slope of the experimental curves plotted in Fig. 6.14. Vapour pressures and Henry constants are ... [Pg.217]

There is one very widely used equation for estimating the vapour pressure of organic liquids, the Antoine equation... [Pg.12]

Vapour pressure equation constants (Logio, mmHg) Antoine equation A... [Pg.20]


See other pages where Vapour Antoine equation is mentioned: [Pg.331]    [Pg.340]    [Pg.184]    [Pg.137]    [Pg.580]    [Pg.18]    [Pg.330]    [Pg.339]    [Pg.285]    [Pg.321]    [Pg.285]    [Pg.408]    [Pg.408]    [Pg.12]   
See also in sourсe #XX -- [ Pg.585 ]




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