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Concentration mass fraction

The diffusion couple discussed above consists of two halves of the same phase. If the two halves are two minerals, such as Mn-Mg exchange between spinel and garnet (Figure 3-5), there would be both partitioning and diffusion. Define the diffusivity in one half (x < 0) to be D, and in the other half (x > 0) to be D. Both and are constant. Let w be the concentration (mass fraction) of a minor element (such as Mn). The initial condition is... [Pg.204]

Fig. 8. Temperature dependence of transmittance for the system of PAAc-PAAm-water solution (at pH 3. 17 adjusted by HCL). Polymer concentration (mass fraction in %) PAAc, 0.5 PAAm, 0.5... Fig. 8. Temperature dependence of transmittance for the system of PAAc-PAAm-water solution (at pH 3. 17 adjusted by HCL). Polymer concentration (mass fraction in %) PAAc, 0.5 PAAm, 0.5...
The shape of the asymmetric S-O bands in the Ci4AO/SDS difference spectra change with composition. The higher frequency shoulder increases in relative intensity as the SDS content decreases. This change indicates that the dilution of SDS in C14AO results in a replacement of the sulfonate-sodium ion interactions with sulfate-amine oxide interactions, since the exact frequency and shape of the complex S-O band depends on the size and location of the hydrated counterion of the sulfate group (4). A weak band due to amine oxide is known to occur near 1200 cm"1. The influence of this band on the vm S-O bandshape can only be observed at the highest amine oxide concentration (mass fraction SDS = 1%) where a low frequency shoulder near 1200 cm"1 is observed in the difference spectra. [Pg.111]

Analysis of mass transfer systems is complicated by the range of units in which gas and liquid concentrations may be defined, e.g. mass concentration, molar concentration, mass fractions, mole fractions, partial pressures, etc. This leads to a wide range of units for the mass transfer coefficient. [Pg.189]

An alternative way of relating concentrations (mass fractions) of individual species to/ is the assumption of chemical equilibrium. An algorithm based on minimization of Gibbs free energy to compute mole fractions of individual species from / has been discussed by Kuo (1986). The equilibrium model is useful for predicting the formation of intermediate species. If such knowledge of intermediate species is not needed, the much simpler approximation of mixed-is-burnt can be used to relate individual species concentrations with/. In order to calculate the time-averaged values of species concentrations the probability density function (PDF) approach is used. [Pg.139]

Enthalpy-Concentration Mass fraction) Ammonia-Water... [Pg.220]

It is therefore not often that an AR may be plotted with temperature on an independent axis (as is the case with concentration, mass fraction, and residence time), and temperature must be accommodated in a different manner. [Pg.105]

The endothermic peak temperature of 66-67 °C was independent of the CS concentration (mass fraction 16.5-60%). The height of the main endothermic peak increased steeply with increasing CS concentration (mass fraction 16.5-40%). However, in CS containing <55% water, the height of the main endothermic peak decreased steeply with increasing CS concentration (40-60%). The second peak area increased and the second peak temperature shifted to the higher temperature side. Powders of CS alone (without added water, moisture content 12.5%) showed a small endothermic peak at about 150 °C. [Pg.219]

Water is flowing into a well-stirred tank at 150 kg/hr and methanol (MeOH) is being added at 30 kg/hr. The resulting solution is leaving the tank at 120 kg/hr. Because of eflfective stirring, the concentration of the outlet solution is the same as that within the tank. There are 100 kg of fresh water in the tank at the start of the operation, and the rates of input and output remain constant thereafter. Calculate the outlet concentration (mass fraction of methanol) after 1 hr. (See Figure 1.3.)... [Pg.15]

Until now two online applications of the blending tanks model have been implemented at the smelter a simulation model estimating the slag concentrate mass fraction in the feed mixture and a Kalman filter estimation of the feed mixture composition. Both models include a shared data reconciliation part, which estimates the masses and mass flows in the process and a shared calculation of state space model parameters according... [Pg.735]

In Fig. 5 the trend is reported of the maximum current intensity of the latter vs. concentration (mass fraction). The different structure-regions encountered are also depicted. [Pg.201]

From a thermodynamic point of view, the state of each chemical species is characterized by the same variables as in non-conductive media (see Chapter 2 of [PRU12]). For example, species k is present at a concentration (mass fraction), a chemical potential per unit mass. The non-polarized conductive medium, with internal energy... [Pg.25]

Description The sensitivity can give information about measurement range and detection power of an instrument. In ICP-MS sensitivity usually is expressed as the measured intensity of a standard solution divided by the concentration (mass fraction, in this case) and extrapolated to a mass fraction of 1 mg/kg. [Pg.149]


See other pages where Concentration mass fraction is mentioned: [Pg.56]    [Pg.474]    [Pg.413]    [Pg.435]    [Pg.148]    [Pg.10]    [Pg.886]    [Pg.888]    [Pg.429]    [Pg.56]    [Pg.245]    [Pg.111]    [Pg.116]   
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Fractional mass

Mass Fraction and Concentration

Mass concentration

Mass fractions

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