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Gases solubility in liquid

In the previous sections, we emphasized that at constant temperature, the liquid-phase activity coefficient is a function of both pressure and composition. Therefore, any thermodynamic treatment of gas solubility in liquids must consider the question of how the activity coefficient of the gaseous solute in the liquid phase varies with pressure and with composition under isothermal conditions. [Pg.166]

Compciring gas solubility in liquids with the concept of vapor pressure highlights another important pattern Increasing pressure increases the solubility of a gas in liquid. Just as high pressures make it more difficult for surface-dwelling liquid molecules to escape into vapor phase, high pressures inhibit the escape of gases dissolved in solvent. Henry s law summarizes this relationship between pressure and gas solubility ... [Pg.176]

In general, gas solubilities in liquids are given by the Henry s law, that is. [Pg.74]

Because ordinary gases, such as O2 or H2 are miscible with SCFs, the limitation of poor gas solubility in liquids is removed. Therefore enzyme-catalyzed... [Pg.414]

Temperature has a greater effect on gas solubility in liquids than it has on solids or liquids dissolving in liquids. Without exception, lower temperatures cause more gas to dissolve in a given volume of liquid. Higher temperatures cause less gas to dissolve. As every fisherman knows, fish prefer deeper water in the summer months. This is because more oxygen dissolves in colder water, and the water temperature is generally cooler at greater depths. [Pg.119]

Other gas solubility units. Depending on the various applications, units such as volume fraction, concentration, molarity, molality and weight fraction have been used to express gas solubility in liquids. For example. [Pg.61]

The factors affecting the precision and accuracy of gas solubility in liquids are numerous. A precision of + 1 % in gas solubility measurements appears to be adequate for most practical and theoretical applications. These factors are ... [Pg.61]

It is to note that there are many versions of commercially and miscellaneous apparatuses available to measure the gas solubility in liquids. [Pg.65]

For industrial applications, it is interesting to study the effect of temperature on gas solubility in liquids Some literature investigations are given. [Pg.70]

We present here some experimental data on gas solubilities in liquids obtained in our laboratory. The liquid previously degassed is saturated by the unreacted gas, in a thermostated autoclave, provided with a mechanically bladed stirrer under a solute partial pressure p. After saturation attainment, a sample of the saturated liquid is taken via a syringe of high precision and injected into a gas-chromatograph in order to extract the solute dissolved in a known volume of the liquid sample V. By the way of calibration gas of known solute mole fraction, the number of... [Pg.73]

Gas solubility in liquid phase is usually very low and therefore it can be a limiting factor influencing the overall reaction rate. Most reactions of interest for the application of three-phase catalytic membrane reactors are hydrogenation reactions using hydrogen and oxidation reactions with air. [Pg.161]

For historical reasons, there are several different ways to express gas solubilities in liquids, such as Bunsen s and Ostwald s coefficients. These are not treated here in detail, and the reader is referred to Refs. [1] and [2]. Nowadays, the most common means to express gas solubilities is to turn to the equilibrium molar fractions or x) of dissolved gas A and to the temperature and pressure of the gas. From the ratio... [Pg.569]

Owing to low gas solubility in liquids the concentration of the gaseous reactant in the liquid phase is usually much smaller than that of the liquid reactant B. As mixing in BCR is usually large. [Pg.416]

Isobaric-isothermal methods are often also called dynamic methods. One or more fluid streams are pumped continuoirsly into a thermostated equilibriirm cell. The pressure is kept constant during the experiment by controlling an effluent stream, irsually of the vapor phase. One can distinguish between continuorrs-flow methods and semi-flow methods. In continuous-flow methods, both phases flow throrrgh the eqrrihbrirrm cell. They can be used only for systems where the time needed to attain phase equilibrium is sufficiently short. Therefore, such equipment is usually not applied to polymer solutions. In semi-flow methods, only one phase is flowing while the other stays in the equilibrium phase. They are sometimes called gas-saturation methods or pure-gas circulation methods and can be used to measure gas solubilities in liquids and melts or solubilities of liquid or solid substances in supercritical fluids. [Pg.3]

From the more practical point of view, what is the basis for developing the analytical description of these equilibrium states In previous Chapters, for example, we accepted that when two phases are in equilibrium at a given temperature and pressure, the fugacity of any component in the one phase is equal to that in the other phase. [We used this equality to arrive at a physical interpretation of fugacity in Chapters 9 and 11 to determine vapor pressures of pure fluids in Chapter 10 using equations of state and to calculate gas solubilities in liquids, or solid and liquid solubilities in compressed gases, in Chapter 11.] Where does this equality of fugacities come from ... [Pg.393]


See other pages where Gases solubility in liquid is mentioned: [Pg.7]    [Pg.368]    [Pg.230]    [Pg.21]    [Pg.407]    [Pg.368]    [Pg.10]    [Pg.63]    [Pg.64]    [Pg.73]    [Pg.1948]    [Pg.247]   
See also in sourсe #XX -- [ Pg.59 , Pg.60 ]




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