Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Partial pressures, law

Dalton s law of partial pressure law which states that the total atmospheric pressure (.Pt) is the sum of all partial pressures (Pt) exerted by each of the gases in the entire mixture of air. [Pg.517]

Volume and Moles Avogadro s Law The Ideal Gas Law Dalton s Law of Partial Pressures Laws and Models ... [Pg.358]

Dalton s law of partial pressures The total pressure (P) exerted by a mixture of gases is equal to the sum of the partial pressures (p) of the components of the gas mixture. The partial pressure is defined as the pressure the gas would exert if it was contained in the same volume as that occupied by the mixture. [Pg.125]

If tire diffusion coefficient is independent of tire concentration, equation (C2.1.22) reduces to tire usual fonn of Pick s second law. Analytical solutions to diffusion equations for several types of boundary conditions have been derived [M]- In tlie particular situation of a steady state, tire flux is constant. Using Henry s law (c = kp) to relate tire concentration on both sides of tire membrane to tire partial pressure, tire constant flux can be written as... [Pg.2536]

Steam Distillation. Distillation of a Pair of Immiscible Liquids. Steam distillation is a method for the isolation and purification of substances. It is applicable to liquids which are usually regarded as completely immiscible or to liquids which are miscible to only a very limited extent. In the following discussion it will be assumed that the liquids are completely immiscible. The saturated vapours of such completely immiscible liquids follow Dalton s law of partial pressures (1801), which may be stated when two or more gases or vapoms which do not react chemically with one another are mixed at constant temperature each gas exerts the same pressure as if it alone were present and that... [Pg.12]

The composition of the vapour can easily be calculated as follows — Assuming that the gas laws are applicable, it follows that the number of molecules of each component in the vapour wdll be proportional to its partial pressure, i.e., to the vapour pressure of the pure liquid at that temperature. If and p are the vapour pressures of the two liquids A and B at the boiling point of the mixture, then the total pressure P is given by ... [Pg.13]

Henry s Law. The solubility of a gas is directly proportional to the partial pressure exerted by the gas ... [Pg.531]

An ideal gas obeys Dalton s law that is, the total pressure is the sum of the partial pressures of the components. An ideal solution obeys Raoult s law that is, the partial pressure of the ith component in a solution is equal to the mole fraction of that component in the solution times the vapor pressure of pure component i. Use these relationships to relate the mole fraction of component 1 in the equilibrium vapor to its mole fraction in a two-component solution and relate the result to the ideal case of the copolymer composition equation. [Pg.429]

The Driving Force for Mass Transfer. The rate of mass transfer increases as the driving force, (7 — (7, is increased. can be enhanced as follows. From Dalton s law of partial pressures... [Pg.333]

The solubihty of a gas in water is affected by temperature, total pressure, the presence of other dissolved materials, and the molecular nature of the gas. Oxygen solubihty is inversely proportional to the water temperature and, at a given temperature, directly proportional to the partial pressure of the oxygen in contact with the water. Under equihbrium conditions, Henry s law apphes... [Pg.339]

Chlorine. The solubiUty of chlorine [7782-50-5] in hydrochloric acid is an important factor in the purification of by-product hydrochloric acid. The concentration of chlorine in solution, S, is proportional to the partial pressure of chlorine, p, in the gas phase and follows Henry s law, S = i/p, in the... [Pg.442]

Other conventions for treating equiUbrium exist and, in fact, a rigorous thermodynamic treatment differs in important ways. Eor reactions in the gas phase, partial pressures of components are related to molar concentrations, and an equilibrium constant i, expressed directiy in terms of pressures, is convenient. If the ideal gas law appHes, the partial pressure is related to the molar concentration by a factor of RT, the gas constant times temperature, raised to the power of the reaction coefficients. [Pg.507]

Titanium tetrachloride is completely miscible with chlorine. The dissolution obeys Henry s law, ie, the mole fraction of chlorine ia a solutioa of titanium tetrachloride is proportional to the chlorine partial pressure ia the vapor phase. The heat of solutioa is 16.7 kJ/mol (3.99 kcal/mol). The appareat maximum solubiUties of chlorine at 15.45 kPa (116 mm Hg) total pressure foUow. [Pg.130]

The equihbrium partitioning of a chemical solute between a Hquid and vapor phase is governed by Henry s law when the Hquid mixture is very dilute in the solute. Henry s law generally is vaHd at concentrations below 0.01 mol/L of solution, although the upper limit can sometimes extend to 0.1 mol/L or higher (10). Over this concentration range, a direct proportionaHty, ie, Henry s constant, is observed between the partial pressure of the chemical in the gas phase and its mole fraction in the Hquid phase. Henry s constant, when expressed in this way, has units of pressure (3). [Pg.235]

In equation 21 the vapor phase is considered to be ideal, and all nonideaHty effects are attributed to the Hquid-phase activity coefficient, y. For an ideal solution (7 = 1), equation 21 becomes Raoult s law for the partial pressure,exerted by the Hquid mixture ... [Pg.235]

The H in solubility tables (2-121 to 2-144) is the proportionahty constant for the expression of Henry s law, p = Hx, mere x = mole fraction of the solute in the liqiiid phase p = partial pressure of the solute in the gas phase, expressed in atmospheres and H = a. proportionality constant expressed in units of atmospheres of solute pressure in the gas phase per unit concentration of the solute in the hquid phase. (The unit of concentration of the solute in the liquid phase is moles solute per mole solution.)... [Pg.169]

When kc and K g values are reported in units (SI) of kmoL/[(s m") (kPa)], one must be careful in converting them to a mole-fracdion basis to multiply by the total pressure actually employed in the original experiments and not by the total pressure or the system to Be designed. This conversion is valid for systems in which Dalton s law of partial pressures p = ypr) is valid. [Pg.602]

For dilute concentrations of manv gases and over a fairly wide range for some gases, the equihbrium relationship is given by Henry s law, which relates the partial pressure developed by a dissolved solute A in a liquid solvent B by one of the following equations ... [Pg.1351]

Although quite useful when it can be apphed, this law should be checked experimentally to determine the accuracy with which it can be used. If Heniy s law holds, the solubility is defined by stating the value of the constant H (or H ) along with the temperature and the solute partial pressure for which it is to be employea. [Pg.1351]

For quite a number of gases, Henry s law holds very well when the partial pressure of the solute is less than about 100 kPa (I atm). For partial pressures of the solute gas greater than 100 kPa, H seldom is independent of the partial pressure of the solute gas, and a given value of H can be used over only a narrow range of partial pressures. There is a strongly nonlinear variation of Heniy s-law constants with temperature as discussed by Schulze and Prausnitz [2nd. Eng. Chem. Fun-dam., 20,175 (1981)]. Consultation of this reference is recommended before considering temperature extrapolations of Henry s-law data. [Pg.1351]

Pure-component vapor pressures can be used for predicting solu-bihties for systems in which RaoiilFs law is valid. For such systems Pa = Pa a, where p° is the pure-component vapor pressure of the solute andp is its partial pressure. Extreme care should be exercised when attempting to use pure-component vapor pressures to predict gas-absorption behavior. Both liquid-phase and vapor-phase nonidealities can cause significant deviations from the behavior predicted from pure-component vapor pressures in combination with Raoult s law. Vapor-pressure data are available in Sec. 3 for a variety of materials. [Pg.1351]

When one pure liquid exists in the presence of another pure liquid, where the liquids neither react nor are soluble in each other, the vapor pressure of one liquid will not affect the vapor pressure of the other liquid. The sum of the partial pressures P is equal to the total pressure P. This relationship is formalized in Dalton s Law, which is expressed as... [Pg.18]


See other pages where Partial pressures, law is mentioned: [Pg.339]    [Pg.17]    [Pg.339]    [Pg.17]    [Pg.742]    [Pg.358]    [Pg.2536]    [Pg.278]    [Pg.432]    [Pg.255]    [Pg.339]    [Pg.254]    [Pg.500]    [Pg.95]    [Pg.95]    [Pg.156]    [Pg.243]    [Pg.237]    [Pg.603]    [Pg.1048]    [Pg.1351]    [Pg.274]    [Pg.222]    [Pg.131]   
See also in sourсe #XX -- [ Pg.93 , Pg.94 , Pg.95 ]

See also in sourсe #XX -- [ Pg.80 , Pg.206 ]

See also in sourсe #XX -- [ Pg.196 , Pg.197 , Pg.198 , Pg.199 ]

See also in sourсe #XX -- [ Pg.23 , Pg.28 ]




SEARCH



Partial pressure

Pressure law

© 2024 chempedia.info