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Liquid solutions sublimation pressure

The relations which are found here will be best understood with the help of Fig. 72 In this figure, OB represents the sublimation curve of ice, and BC the vaporisation curve of water the curve for the solution must lie below this, and must cut the sublimation curve of ice at some temperature below the melting-point. The point of intersection A is the cryohydric point. If the solubility increases with rise of temperature, the increase of the vapour pressure due to the latter will be partially annulled. Since at first the effect of increase of temperature more than counteracts the depressing action of increase of concentration, the vapour pressure will increase on raising the temperature above the cryohydric point. If the elevation of temperature is continued, however, to the melting-point of the salt, the effect of increasing concentration makes itself more and more felt, so that the vapour-pressure curve of the solution falls more and more below that of the pure liquid, and the pressure will ultimately become equal to that of the pure salt that is to say, practically equal to zero. The curve will therefore be of the general form AMF shown in Fig. 72. If the solubility should diminish with rise of temperature, the two factors, temperature and concentration, will act in the same direction, and the vapour-pressure curve will rise relatively more rapidly than that of the pure liquid since, however, the pure salt is ultimately obtained, the vapour-pressure curve must in this case also finally approach the value zero.2... [Pg.171]

Steroid Hormones and Other Steroidal Synthetics Sublimation Pressure for Organic Compounds Surface Tension of Liquid Elements Temperature Correction for Barometer Readings Temperature Correction for Glass Volumetric Apparatus Temperature Correction for Volumetric Solutions Temperature Correction, Glass Scale... [Pg.2698]

The phase behavior and solubility of soHds in supercritical fluids is quite different than that in liquids. First, it is assumed that the solubility of the fluid-phase component, such as supercritical CO2, in the solid phase is negligible. This is unlike the equihbrirmi with liquids, where one must consider the mutual solubilities of both the liquid solute and the fluid phase. From thermodynamics, the mole fraction solubility of a solute in a supercritical fluid, y2, is given by Eq. (4), where, P is the sublimation pressure of the solid which is a function of temperature alone, the exponential term is called the Poynting correction (usual values are 1 to 4) to account for hydrostatic pressure, and the fugacity coefficient, ]>, which accounts for the non-idealities of the fluid phase at a certain temperature, pressure, and concentration. At low pressures, the behavior is ideal and the solubility y2 is equal to P /P. [Pg.617]

An increase in the boiling point or a decrease in the freezing point of a solution containing a nonvolatile component is compared to pure solvent caused by a reduction in the vapor pressure. The reduction of the freezing point AT of a solution is T — T, as shown in Fig. 1-42 where T is the freezing point (or melting point) of the pure solvent. At Tg the vapor pressure is the same for the liquid and solid phases of the solvent. Tg is defined by the intersection A of the vapor pressure curve VC and the sublimation pressure curve SC of the solvent. If only pure solvent freezes, the freezing point T of the solution occurs at the intersection B of the vapor pressure curve of the solution VCS and the sublimation pressure curve of the solvent SC. [Pg.63]

From Eq. (13), solubility expressed in mole fraction of the solid x, is dependent on the heat of fusion A which can be related to the sublimation pressure P " of the solid, and the melting temperature Pm (exactly triple-point temperature Prr) of the solid. Assuming an ideal solution, with an activity coefficient /i of unity, the solubility of a solid in a liquid can be calculated. In the present case, the magnitude of separation of two species will depend principally on the difference in their melting temperatures (APm = Pmi — 7m2). Modifying the solvent will produce a nonideal solution with activity coefficients different from unity. In such a case, separation is also dependent on the difference in activity coefficient of both species (A/ = /i - /2). [Pg.464]

At a temperature below its freezing point of 2.0 °C, the hydrazine will be present as a solid in equilibrium with its vapor. We are seeking the sublimation pressure of N2H4(s) at the melting point of ice, 0 °C. At its freezing point of 2.0 "C, the hydrazine coexists in three phases—liquid, solid, and vapor. We must first determine the vapor pressure of hydrazine at 2.0 °C. Then we can then use the Clausius-Clapeyron equation (12.2) to calculate the vapor (sublimation) pressure at 0 "C. Our principal task will be to identify the data needed to apply the Clausius-Clapeyron equation, three times in all, as detailed in the stepwise solution to the problem. [Pg.566]

B. Di-tert-butyl dicarbonate. A solution of 20.0 g. (0.076 mole) of di-i-butyl tricarbonate in 75 ml. of carbon tetrachloride is placed in a 600-ml. beaker fitted with a magnetic stirrer, and 0.10 g. (0.0009 mole) of freshly sublimed l,4-diazabicyclo[2.2.2]octane (DABCO) is added (Note 9). Rapid evolution of carbon dioxide begins at once. The reaction mixture is stirred at 25° for 45 minutes to complete the loss of carbon dioxide (Note 10), and then 35 ml. of water, containing sufficient citric acid to make the aqueous layer slightly acidic, is added. The layers are separated and the organic layer is dried over anhydrous magnesium sulfate and then concentrated at 25° with a rotary evaporator. The residual liquid is distilled under reduced pressure to separate 13.3-15.1 g. (80-91%) of di-butyl dicarbonate as a colorless liquid, b.p. 55-56° (0.15 mm.) or 62-65° (0.4 mm.) n T> 1.4071-1.4072 (Note 11). [Pg.47]

If A is a gas at ambient temperature and pressure, AsoiVH° can be determined experimentally by calorimetric methods or from measurements of the solubility change with temperature [42-44], When A is a liquid or a solid, its solvation enthalpy in a given solvent is usually calculated from its standard solution enthalpy (Asin//°) and its standard vaporization or sublimation enthalpy ... [Pg.26]

White monoclinic crystals density 5.09 g/cm melts at 64°C (triple point) sublimes at 56.6°C critical temperature 232.65°C critical pressure 46 atm critical volume 250 cm /mol reacts with water forming UO2F2 and HF soluble in chloroform, carbon tetrachloride and fluorocarbon solvents soluble in liquid chlorine and bromine dissolves in nitrobenzene to form a dark red solution that fumes in air. [Pg.960]

Most tanks store liquid rather than gases or solids. Characteristics and properties such as corrosiveness, internal pressures of multicomponent solutions, tendency to scale or sublime, and formation of deposits and sludges are vital for the tank designer and the operator of the tank and are discussed herein. Excluded from the discussion are the unique properties and hazards of aerosols (qv), unstable liquids, and emulsions (qv). A good source of information for liquid properties for a wide range of compounds is available (2). [Pg.308]

Gallic acid is heated with about half its weight of water in a copper autoclave until the pressure reaches 1.2 MPa (12 atm) and the temperature is 175°C. Steam and carbon dioxide are released but sufficient water is retained to maintain the pyrogallol as a liquid. The cooled solution is decolorized with animal charcoal and is then evaporated until the volatile pyrogallol distills into iron receivers. The solidified material is purified by repeated distillation, sublimation, or vacuum distillation at 200°C in the presence of dialkyl phthalates (8). [Pg.377]

When a solution freezes, the solid is usually pure solvent. Thus the solid-vapor equilibrium (sublimation) P-T curve is unaffected by the presence of solute. The intersection of this curve and the liquid-vapor curve is the triple point (nearly the same temperature as the freezing point, which is measured at atmospheric pressure). Since a solute lowers the solvent vapor pressure, the triple point is shifted to lower temperature, as shown in Figure 11-2. Detailed calculations show that the decrease in freezing point for a dilute solution is proportional to the total molal concentration of solutes... [Pg.120]

At room temperature, pentamethylarsorane is a colorless liquid of a characteristic odor which resembles the analogous antimony compound. It crystallizes below — 6°C and can be sublimed under reduced pressure at — 10°C. The (CH3)5As is a monomer in benzene solution and shows a molecular ion in the mass spectrum with very low intensity. The vibrational spectra, infrared and Raman, could be assigned to a trigonal-bipyramidal skeleton. There are striking similarities to the spectra of Sb(CH3)6 (IS). [Pg.230]


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See also in sourсe #XX -- [ Pg.284 , Pg.372 ]




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Sublimate Liquid

Sublimation

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Sublime

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