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Hydrocarbon formation, mole fraction

Ideal Adsorbed Solution Theory. Perhaps the most successful approach to the prediction of multicomponent equiUbria from single-component isotherm data is ideal adsorbed solution theory (14). In essence, the theory is based on the assumption that the adsorbed phase is thermodynamically ideal in the sense that the equiUbrium pressure for each component is simply the product of its mole fraction in the adsorbed phase and the equihbrium pressure for the pure component at the same spreadingpressure. The theoretical basis for this assumption and the details of the calculations required to predict the mixture isotherm are given in standard texts on adsorption (7) as well as in the original paper (14). Whereas the theory has been shown to work well for several systems, notably for mixtures of hydrocarbons on carbon adsorbents, there are a number of systems which do not obey this model. Azeotrope formation and selectivity reversal, which are observed quite commonly in real systems, ate not consistent with an ideal adsorbed... [Pg.256]

A closer analysis of die equilibrium products of the 1 1 mixture of methane and steam shows the presence of hydrocarbons as minor constituents. Experimental results for die coupling reaction show that the yield of hydrocarbons is dependent on the redox properties of the oxide catalyst, and the oxygen potential of the gas phase, as well as die temperamre and total pressure. In any substantial oxygen mole fraction in the gas, the predominant reaction is the formation of CO and the coupling reaction is a minor one. [Pg.142]

Studies concerning the micelle formation/breakdown in mixed micellar solutions are few. Folger et al. showed that small amounts of STS (mole fraction 2-5%) significantly affected the value of T2 for SDS, particularly at C close to the cmc (see Figure 3.5). This is expected since micelle formation/breakdown is similar to a nucleation process. Patist et ai 160 reported that the slow relaxation process in solutions of SDS became considerably slower upon the addition of alkyl-trimethylammonium bromides. The largest effect was obtained with dodecyltrimethylammonium bromide, and the authors interpreted the results in terms of chain compatibility. Measurements of the slow relaxation time have been used to show that solutions of mixtures of some hydrocarbon and perfluorocarbon surfactants contain two types of mixed micelles, one rich in hydrocarbon surfactant, the other rich in perfluorocarbon surfactant. [Pg.118]

When air is used to clear a line that had contained hydrocarbons, the potential for forming a flammable mixture of air with hydrocarbon vapors and/or mist is created. The elevated pressure which can be developed in a line or system broadens the flammable range, lowers the autoignition temperature, and can convert a previously fuel-rich mixture into a flammable mixture by lowering the vapor mole fraction of the fuel. Even though the temperature of a hydrocarbon liquid in a line may be below its flash point, mist formation can occur due to the sparging action of the air and can result in a flammable quantity of material being forced into the vapor space. [Pg.62]

The critical micelle concentrations of mixtures of POE nonionic surfactants are of particular interest, since the synthesis of such materials on a commercial basis will always produce a rather broad range of POE chain lengths. Because they contain no electrostatic contribution to the free energy of micelle formation, they can be treated theoretically with a simpler relationship between composition and cmc. In a mixture of nonionic surfactants in which the average POE chain lengths are approximately the same and the hydrocarbon chains different, there was a smooth decrease in the cmc of the mixture as the mole fraction of the more hydrophobic material (lower cmc) was increased, reminiscent of the surface tension-mole fraction curves found for miscible organic materials mixed with water. [Pg.151]


See other pages where Hydrocarbon formation, mole fraction is mentioned: [Pg.529]    [Pg.101]    [Pg.130]    [Pg.127]    [Pg.173]    [Pg.23]    [Pg.38]    [Pg.245]    [Pg.270]    [Pg.123]    [Pg.68]    [Pg.73]    [Pg.519]    [Pg.291]    [Pg.91]    [Pg.83]    [Pg.31]   


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Hydrocarbon fractions

Hydrocarbons, fractionation

Mole fraction

Moles mole fraction

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