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Vapor equilibrium and

Many reactions, however, do not run to completion. They will reach a point where they stop, but in this chapter you will learn that when they are in this state they are not really stopped at all. These reactions, where the products can readily reform the reactants, are known as reversible reactions. The way these reactions proceed is analogous to the systems in equilibrium that were discussed in Chapters 8 and 10 (vapor equilibrium and solutions). In the next three chapters, you will study the equilibrium of chemical reactions and learn more about the factors associated with it. The focus of this chapter is to introduce the equilibrium constant, which provides data about the relationships between reactants and products in a system at equilibrium, and Le Chatelier s Principle, which allows you to predict the effects of different stressors on reaction equilibria. [Pg.291]

Other interactions in a membrane internal nanospace. The first is evaporation through a nonporous membrane (pervaporation). Interaction of separating components with a polymer in a membrane internal nanospace, in some cases, moves liquid-vapor equilibrium and removes azeotropic points. [Pg.15]

Ait-Kaci, A. Belaribi, G. Michou-Saucet, C. Jose, J. liquid-vapor equilibrium and excess Gibbs eneigy of 1-hexyne + heptane Int. DATA Ser., Sel. Data Mixtures, Set. A 1992,20,32-34... [Pg.344]

Uncertainties (T(.x ) = 0.0002 c7(P)/103Pa = 0.009 ctQi) -Berro, C. Excess volume, liquid-vapor equilibrium, and excess Gibbs energy of 1-alkanols (C2-C4 +, ... [Pg.1152]

Oracz, P. Liquid-vapor equilibrium and excess Gibbs energy of 2-methyl-2-propanol + benzene, + toluene, + ethylbenzene, or + 1,4-dimethylbenzene hit. DATA Ser., Sel. Data Mixtures, Ser. A 1989,17,241-252... [Pg.1444]

Cocero, M. J. Gonzalez, J. A. Garcia, I. Cobos, J. C. Mato, F. Liquid-vapor equilibrium and excess Gibbs energy of diethyl... [Pg.1723]

Ait-Kad, A. Belarihi, B. F. Jose, J. Liquid-vapor equilibrium and excess Gibbs energy of binary mixtures containing oxane, 1,4-dioxane, or piperidine Int. DATA Sen, Sel. Data Mixtures, Sen A 1992, 20, 35-44... [Pg.2156]

Dohnal, V. Vesely, F. Vins, J. Liquid-vapor equilibrium and heats of mixing in the 1-propanol - acetonitrile system Collect. Czech. Chem. Commun. 1982,47,3188-3198... [Pg.3097]

This model, which yields excellent results for polar and non-polar molecular liquids, is especially well suited for the study of liquid/ vapor equilibrium and the equilibrium between two liquids that are not completely miscible. Regardless of the number of components of the solution, the application of this model only requires the knowledge of two adjustment parameters per binary system, which can be deduced from the solution. The model is so widely applicable that it actually contains a number of previously classic models such as the models put forward by Van Laar, Wilson, Renon et al. (the NRTL - Non Random Two Liquids -model), Scatchard and Hildebrand, Flory and Huggins as special cases. In addition, it lends a physical meaning to the first three coefficients P, 5 and , in the Margules expansion (equation [2.1]). [Pg.101]

The water pressure is given by the constant of the solid —vapor equilibrium and thus ... [Pg.703]


See other pages where Vapor equilibrium and is mentioned: [Pg.859]    [Pg.169]    [Pg.496]    [Pg.115]    [Pg.293]    [Pg.736]    [Pg.1150]    [Pg.351]   
See also in sourсe #XX -- [ Pg.483 , Pg.488 ]




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