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Water-alcohol binary mixture

Theoretical results for the solution phase are somewhat different from the experimental results in the gas phase. In the solution phase we do have extensive clustering among DMSO molecules but that starts around 14-15% of DMSO. [Pg.249]

Most common water-alcohol mixtures are water-methanol and water-ethanol solutions. Mixtures of water with other alcohols higher in the series (such as propanol and butanol) are also common. Water-phenol mixtures are also routinely used in laboratories and surgical procedures as a disinfectant. [Pg.249]

Water-alcohol mixtures act as good solvents because they can solvate organic solutes which are not usually soluble in water. They can also solvate ions which are sometimes soluble in alcohols. [Pg.249]


The surface excess isotherm for adsorption of bulk water (0 < Xi < 1) from a binary liquid mixture can be U (water selectively adsorbed at all values of Xi) or S (water not selectively adsorbed at aU values of xi) shaped [20], Figure 8 shows an example of U shaped isotherm for adsorption of water-alcohol binary mixture on Alcoa H-152 alumina... [Pg.639]

The use of a ternary mixture in the drying of a liquid (ethyl alcohol) has been described in Section 1,5 the following is an example of its application to the drying of a solid. Laevulose (fructose) is dissolved in warm absolute ethyl alcohol, benzene is added, and the mixture is fractionated. A ternary mixture, alcohol-benzene-water, b.p. 64°, distils first, and then the binary mixture, benzene-alcohol, b.p. 68-3°. The residual, dry alcoholic solution is partially distilled and the concentrated solution is allowed to crystallise the anhydrous sugar separates. [Pg.144]

Example Separation of 2-Propanol—Water. Consider the separation of a binary mixture of 60 mol % water and 40 mol % 2-propanol (or isopropyl alcohol (IPA)) into two products consisting of 2-propanol of 99.5 mol % purity and water with <100 ppm 2-propanol impurity. [Pg.453]

The first successful appHcation of heterogeneous azeotropic distillation was in 1902 (87) and involved using benzene to produce absolute alcohol from a binary mixture of ethanol and water. This batch process was patented in 1903 (88) and later converted to a continuous process (89). Good reviews of the early development and widespread appHcation of continuous azeotropic distillation in the prewar chemical industry are available (90). [Pg.190]

Let us take the general case in which both phases are binary mixtures, and suppose, first, that the system consists of a mixture of two liquids, say alcohol and water, in contact with the vapour. [Pg.415]

Jso-propyl alcohol is very difficult to dry satisfactorily. The water binary mixture, boiling at 80.35°, contains 12.1 per cent of water by weight. The ternary mixture with benzene, boiling at 66.5°, contains 73.8 per cent benzene, 18.7 per cent iso-propyl alcohol and 7.5 per cent water. Hence by adding 120 g. of dry benzene to 100 g. of the iso-propyl-water binary, and distilling off until the temperature reaches 82°, there will remain 55 to 60 g. of nearly dry iso-propyl alcohol. The commercial anhydrous alcohol was used in this preparation. [Pg.108]

One of the added merits of batch distillation is that more than one product may be obtained. Thus, a binary mixture of alcohol and water may be distilled to obtain initially a high quality alcohol. As the composition in the still weakens with respect to alcohol, a second product may be removed from the top with a reduced concentration of alcohol. In this way it is possible to obtain not only two different quality products, but also to reduce the alcohol in the still to a minimum value. This method of operation is particularly useful for handling small quantities of multi-component organic mixtures, since it is possible to obtain the different components at reasonable degrees of purity, in turn. To obtain the maximum recovery of a valuable component, the charge remaining in the still after the first distillation may be added to the next batch. [Pg.593]

Reversed-phase chromatography employs a nonpolar stationary phase and a polar aqueous-organic mobile phase. The stationary phase may be a nonpolar ligand, such as an alkyl hydrocarbon, bonded to a support matrix such as microparticulate silica, or it may be a microparticulate polymeric resin such as cross-linked polystyrene-divinylbenzene. The mobile phase is typically a binary mixture of a weak solvent, such as water or an aqueous buffer, and a strong solvent such as acetonitrile or a short-chain alcohol. Retention is modulated by changing the relative proportion of the weak and strong solvents. Additives may be incorporated into the mobile phase to modulate chromatographic selectivity, to suppress undesirable interactions of the analyte with the matrix, or to promote analyte solubility or stability. [Pg.28]

It will be observed that the F, N curves for such binary mixtures follow the same course—a rapid followed by a more gentle rise of F as iV increases to a well defined maximum followed by a drop and an asymptotic fall in the F value. In the case of alcohol water mixtures F ax. is obtained at about 0 3A. To find an adequate explanation for the complete F, N curve is by no means an easy matter. It is clear that the first portion of the curve may be taken to represent an increasing surface concentration of alcohol and this proceeds to a limiting value—an observation first made by Milner (Phil. Mag. xill. 96, 1907), who showed that for relatively strong solutions of acetic acid the surface tension of the solutions could be expressed as a function of the concentration of the acetic acid in the following form ... [Pg.41]

A mathematical procedure for the design of fractionating towers developed by Sorel (54) in 1893 had little acceptance by the petroleum industry because it was based on treatment of binary mixtures, such as alcohol and water the required vapor-liquid data on petroleum products were in general not available the calculations were laborious the original publication was in French and not widely available to American industry and the builders of refinery equipment were seldom staffed to use the procedure. [Pg.205]

Vapor-liquid equilibrium data at atmospheric pressure (690-700 mmHg) for the systems consisting of ethyl alcohol-water saturated with copper(II) chloride, strontium chloride, and nickel(II) chloride are presented. Also provided are the solubilities of each of these salts in the liquid binary mixture at the boiling point. Copper(II) chloride and nickel(II) chloride completely break the azeotrope, while strontium chloride moves the azeotrope up to richer compositions in ethyl alcohol. The equilibrium data are correlated by two separate methods, one based on modified mole fractions, and the other on deviations from Raoult s Law. [Pg.91]

Colourless liquid spirituous odour miscible with water in all proportions binary mixture with water contains 75-57% alcohol, and boils at 78-1° at 760 mms. B.P. 760 pure alcohol, 78-3° B.P. 2113° D. 0-790. It forms a ternary mixture with benzene and water, and this property is utilised in the manufacture of industrial absolute alcohol. (J. C. S., 81, 707 see Preparation 198 B., 38, 3612.)... [Pg.214]

Capello et al.16 also assessed the environmental impacts of the life cycles of four solvent mixtures (methanol-water, ethanol-water, methanol-ethanol, and -propyl alcohol-water of different compositions w/w) that can be used for the solvolysis of p-methoxybenzoyl chloride. Different waste treatment scenarios for these binary mixtures (incineration and distillation) were analyzed. It appears that a solvent mixture with a high water content has a low environmental impact because the cumulative energy demand (CED) for the production of water is about three orders of magnitude lower than that for organic solvents.37... [Pg.426]

Figure 3.9 highlights the key feature of a RCM by means of the mixture isopropanol, n-propanol, water, in which two binary azeotropes of water-alcohol occur ... [Pg.85]

The relations between the r were worked out for binary, slightly volatile solutions and numerical values calculated for water-alcohol mixtures. The general relations are... [Pg.123]

For binary mixtures of ethyl alcohol and water the following values have been obtained 1... [Pg.116]

In this chapter we will first discuss coherent anti-Stokes Raman scattering (CARS) of simple liquids and binary mixtures for the determination of vibrational dephasing and correlation times. The time constants represent detailed information on the intermolecular interactions in the liquid phase. In the second section we consider strongly associated liquids and summarize the results of time-resolved IR spectroscopy (see, e.g., Ref. 17) on the dynamics of monomeric and associated alcohols as well as isotopic water mixtures. [Pg.16]

Very high maxima occur with binary mixtures of several organic liquids (alcohol, acetic acid, etc.) with water, i Jones and Veazeyi considered that association is reduced on mixing two associated liquids, whilst Dunstan and Thole 18 assumed further association, and eventually complex formation, on mixing. This question, the answer to which is still undecided, is discussed by... [Pg.116]


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