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Binary mixtures amount

Katz, Lochmuller and Scott also examined acetonitrile/water, and tetrahydrofuran (THF)/water mixtures in the same way and showed that there was significant association between the water and both solvents but not nearly to the same extent as methanol/water. At the point of maximum association for methanol, the solvent mixture contained nearly 60% of the methanol/water associate. In contrast the maximum amount of THF associate that was formed amounted to only about 17%, and for acetonitrile the maximum amount of associate that was formed was as little as 8%. It follows that acetonitrile/water mixtures would be expected to behave more nearly as binary mixtures than methanol/water or THF/water mixtures. [Pg.133]

In the previous sections, we indicated how, under certain conditions, pressure may be used to induce immiscibility in liquid and gaseous binary mixtures which at normal pressures are completely miscible. We now want to consider how the introduction of a third component can bring about immiscibility in a binary liquid that is completely miscible in the absence of the third component. Specifically, we are concerned with the case where the added component is a gas in this case, elevated pressures are required in order to dissolve an appreciable amount of the added component in the binary liquid solvent. For the situation to be discussed, it should be clear that phase instability is not a consequence of the effect of pressure on the chemical potentials, as was the case in the previous sections, but results instead from the presence of an additional component which affects the chemical potentials of the components to be separated. High pressure enters into our discussion only indirectly, because we want to use a highly volatile substance for the additional component. [Pg.194]

We consider a binary liquid mixture of components 1 and 3 to be consistent with our previous notation, we reserve the subscript 2 for the gaseous component. Components 1 and 3 are completely miscible at room temperature the (upper) critical solution temperature Tc is far below room temperature, as indicated by the lower curve in Fig. 27. Suppose now that we dissolve a small amount of component 2 in the binary mixture what happens to the critical solution temperature This question was considered by Prigogine (P14), who assumed that for any binary pair which can be formed from the three components 1, 2 and 3, the excess Gibbs energy (symmetric convention) is given by... [Pg.195]

Within our laboratory we have shown that using the combination of PyMS and ANNs it is possible to follow the production of indole in a number of strains of E. coli grown on media incorporating various amounts of tryptophan,98 and to estimate the amount of casamino acids in mixtures with glycogen.99 It was also shown that it is possible to quantify the (bio)chemical constituents of complex binary mixtures of proteins and nucleic acids in glycogen, and to measure the concentrations of binary and tertiary mixtures of Bacillus subtilis, Escherichia coli, and Staphylococcus aureus.93,100... [Pg.331]

Binary mixtures of glass ballotini and steel beads of nearly equal size (-500 pm and -275 pm, respectively) also exhibit reduced electrostatic activity, as measured by suspended electrodes (Guardiolaet al., 1992). The highly conducting steel beads were added to the glass particles in amounts up to approximately 10% by volume. [Pg.836]

Small amounts of impurities have a significant effect on the refractive index. In fact, the refractive index for many binary mixtures changes linearly with concentration over a wide range of concentrations. A calibration curve of refractive index vs. concentration along with the refractive index of a sample can be used to find the concentration of a species in the sample. For example, the food and beverage industry uses the refractive index to find the concentration of sugar solutions. Table 15.1 lists several additional applications for refractive index. [Pg.427]

These studies have been recently extended to the reaction of n-butylamine (di-BA) and piperidine (PIP) with other aromatic substrates, such as l-chloro-2,4-dinitrobenzene (CDNB) and 4-chloro-3-nitrotrifluoromethylbenzene (CNTFB) in hexane, benzene, mesitylene and binary mixtures of hexane with the aromatic solvents, and the results are consistent with Scheme 4 which includes the proposal of a preferential solvation with the donor solvent, D115. As expected, a decrease in rate was observed in the reactions with butylamine with increasing amounts of the donor solvent, which was attributed to the formation of the EDA complex with the solvent. The result is expressed by equation 18 which, in the limiting case where Ks [Pg.1247]

Adopting a subregular Margules model for the NaAlSi30g-KAlSi308 (Ab-Or) binary mixture and assuming that the activity coefficient of the albite component is not affected by the presence of limited amounts of the third component in the mixture (i.e., CaAljSijOg), equation 5.260 may be transformed into... [Pg.391]

The total monomer concentration of a binary mixture o-f two similarly structured sur-factants o-f like charge (an ideal system) lies between the CMC s o-f the individual sur-factants involved -for total sur-factant concentrations at or above the mixture CMC. Analogously, the vapor pressure of a mixed ideal liquid is intemediate between the vapor pressures of the components of which it is composed, whether there is substantial liquid present or the system is at the dew point (where an infintesimal amount of liquid is present). [Pg.6]

Fig. 4.4 Theoretical calibration plots for absolute peak current (left) in binary mixtures when the amount of mixture is constant for each measurement, and corresponding plots for the percentage peak current (right) [228]... Fig. 4.4 Theoretical calibration plots for absolute peak current (left) in binary mixtures when the amount of mixture is constant for each measurement, and corresponding plots for the percentage peak current (right) [228]...
For binary mixtures the calculated value of Q is directly proportional to the amount of each component and their individual Q values as shown in Equation 5.19,... [Pg.96]

We can start, as did the ancient craftsmen, with the fusion of the iron oxide, FeO, with silica, SiO . The phase diagram for those binary mixtures show that whereas Si02 fuses at about 1713 C and FeO at 13 9 C, mixtures containing between 20 and 40 weight percent FeO fuse below 1250 C. Complexing with additions of another iron oxide, Fe203, in amounts of up to 10%, can lower the fusion temperature to about 1150 C. [Pg.262]

As a mixture of substances is evaporated, the residue becomes relatively depleted in the more volatile constituents. A relation for binary mixtures due to Rayleigh is developed as follows The differential material balance for a change dL in the amount of liquid remaining is... [Pg.378]

Electrolytic (coukxnetric) hygrometers The quantity of electricity required to carry out a chemical reaction is measured. The principle is based upon Faraday s law of electrolysis. Water is absorbed on to a thin film of dessicant (e.g. P2O5) and electrolysed. The current required for the electrolysis varies according to the amount of water vapour absorbed. The current depends also upon the flowrate. Capable of high precision. Used in the range 1000 to 3000 ppm of water by volume. Somewhat complicated procedure. Recombination of products to water is necessary after electrolysis. Density, pressure and flowrates have to be maintained precisely. Contamination can poison the cell. It is ideal for binary mixtures but is of limited range. Suitable for on-line operation. [Pg.520]

Solid-11quid-gas (SLG) equilibrium temperatures and pressures were measured in a constant-volume view cell. A known amount of porphyrin was loaded into the cell, which was then attached to the solvent delivery system and heated to the desired operating temperature. Once thermal equilibrium was obtained, solvent was metered into the cell until the pressure within the cell reached the SLG pressure. Equilibrium was obtained when the pressure stablized and all three phases could be observed. This pressure and the corresponding temperature were recorded as one point on the SLG equilibrium line for the binary mixture. Additional points were obtained by setting a new temperature and repeating the procedure. [Pg.139]

The relative amount of each latex (Vj, Vg) in the different blends, as determined by HDC are shown in Figures 2 and 3. There was excellent correlation between the actual and the measured quantities of each component in the different binary mixtures. This calibration for particle-size distribution demonstrated that the computerized HDC could be used to determine the relative amount of each latex in the various binary mixtures within IX. [Pg.273]

The computerized HDC technique was used to quantify the relative amounts of the large 2100A and small 700A monodisperse latexes in different binary mixtures. The HDC measurements for the relative amounts of the two components were within 1% of the actual amounts. [Pg.286]

For binary mixtures Converse and Huber (1965) found that in all cases studied, column holdup causes a decrease in the amount of maximum distillate obtained for a fixed time of operation. In another way, for a fixed amount of distillate and purity of the lighter component, higher column holdup increased the batch time. The authors concluded that the presence of significant holdup is bad anyway. [Pg.37]


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See also in sourсe #XX -- [ Pg.248 ]




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Binary mixture

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