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Boiling Point Calculations

When heating a liquid consists of two or more components, the bubble point is the point where the first bubble of vapor is formed. Given that vapor will probably have a different composition in the liquid, the bubble point and the dew point at different compositions which provide useful data when designing distillation systems. For single-component mixtures the bubble point and the dew point are the same and are referred to as the boiling point. At the bubble point, the following relationship holds  [Pg.2]

K is the distribution coefficient or K factor, defined as the ratio of mole fraction in the vapor phase i/ to the mole fraction in the liquid phase x at equilibrium. When Raoult s law and Dalton s law hold for the mixture, the K. factor is defined as the ratio of the vapor pressure to the total pressure of the system [2]  [Pg.2]


In freezing-point depression and boiling-point elevation problems, to find the actual freezing/boiling point, calculate the AT (change in temperature), then subtract that amount from the solvent s freezing point, or add it to the solvent s boiling point. [Pg.188]

If you ve been given the boiling point, calculate the ATg by subtracting the boiling point of the pure solvent from the number you were given. If you know the freezing point, add the freezing point of the pure solvent to it to get the ATJ. [Pg.190]

The boiling point calculated from the vapour tension curve is 410° C. [Pg.323]

Six hundred pounds of 10% NaOH per hour at 200"F are added to 400 Ib/hr of 50% NaOH at the boiling point. Calculate the following ... [Pg.477]

Boiling Point, calculated from rates of evaporation of solid tungsten. [Pg.30]

The difference between normal boiling point calculated from the equation reported in the original source and that corresponding to the equation with the parameters reported here is less than 5% (rating C). [Pg.259]

The procedure for boiling point calculation is as follows. Firstly, a temperature t is estimated. Secondly, the vapor pressure of the mixture is calculated fit>m... [Pg.241]

Only one of the vacuum residues (sample 1) has a substantial evapoiizable fraction, as has already been shown using thermogravimetiy (n % = 181 °C, TS % = 237 °C, AG4(X) = 44 wt%). The boiling point, calculated from the DSC peak maximum temperatures and reduced to atmospheric conditions, is 410 °C. [Pg.169]

A further resource is Ref. 3, Appendix 2, Table A 2—2, in which more than 800 binary homogeneous azeotropes are listed. For each azeotrope the following information is supplied the type of homogeneous azeotrope (boiling point suppression, elevation, or neither) its weight composition, boiling point, calculated density, calculated HSP values notation of an absence of measured flash point and some literature or patent references. The table is sorted by total solubility parameter (Hildebrand). [Pg.169]

Prop. bi4 115° (2697), empirical equation for boiling point calculation... [Pg.188]


See other pages where Boiling Point Calculations is mentioned: [Pg.77]    [Pg.63]    [Pg.36]    [Pg.28]    [Pg.268]    [Pg.829]    [Pg.2]    [Pg.191]    [Pg.191]    [Pg.193]    [Pg.194]    [Pg.201]    [Pg.203]    [Pg.476]   


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