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Transport in melts

The phase equilibria of the most important compounds will be described in the following section. In the sections thereafter, we will treat mass transport in melt-phase polycondensation, as well as in solid-state polycondensation, and discuss the diffusion and mass transfer models that have been used for process simulation. [Pg.72]

Figure 11. Representation of a stagnant film in solute transport in melt growth. The variables are defined in the text. Figure 11. Representation of a stagnant film in solute transport in melt growth. The variables are defined in the text.
Mullins and Sekerka (88, 89) analyzed the stability of a planar solidification interface to small disturbances by a rigorous solution of the equations for species and heat transport in melt and crystal and the constraint of equilibrium thermodynamics at the interface. For two-dimensional solidification samples in a constant-temperature gradient, the results predict the onset of a sinusoidal interfacial instability with a wavelength (X) corresponding to the disturbance that is just marginally stable as either G is decreased... [Pg.81]

Electrical Moderate insulators. Conduction by ion transport in melt. Sometimes soluble in liquids of high dielectric constant Insulators in solid and melt Conduction by electron transport Insulators... [Pg.116]

Another method is to start with lactams. The cyclic lactams have a lower melting temperature compared to co-ammo acids and are therefore more easily purified and easier to handle. e-Caprolactam has a melting temperature of 69°C and can be transported in the molten state in heated tanks. The energy consumption of the lactam polymerization is also low as little water is added by the polymerization process and therefore there is little to evaporate. [Pg.174]

In this description the temperature field has been taken to be linear in the coordinate y and to be independent of the shape of the melt/crystal interface. This is a good assumption for systems with equal thermal conductivities in melt and crystal and negligible convective heat transport and latent heat release. Extensions of the model that include determination of the temperature field are discussed in the original analysis of Mullins and Sekerka (17) and in other papers (18,19). [Pg.301]

Diffusion of ions can be observed in multicomponent systems where concentration gradients can arise. In individnal melts, self-diffnsion of ions can be studied with the aid of radiotracers. Whereas the mobilities of ions are lower in melts, the diffusion coefficients are of the same order of magnitude as in aqueous solutions (i.e., about 10 cmVs). Thus, for melts the Nemst relation (4.6) is not applicable. This can be explained in terms of an appreciable contribntion of ion pairs to diffusional transport since these pairs are nncharged, they do not carry cnrrent, so that values of ionic mobility calculated from diffusion coefficients will be high. [Pg.133]

Spiegelman M, (1996) Geochemical conseqnences of melt transport in 2-D the sensitivity of trace elements to mantle dynamics. Earth Planet Sci Lett 139 115-132 Spiegelman M, Kelemen PB, Aharonov E (2001) Canses and consequences of flow organization dnring melt transport The reaction infiltration instability in compactible media. J Geophys Res 106 2061-2077... [Pg.211]

In contrast to the full equilibrium transport model, melt could be incrementally removed from the melting solid and isolated into channels for melt ascent. This model is the disequilibrium transport model of Spiegelman and Elliott (1993). Instead of substituting Equation (A7) in for Cs, the problem becomes one of separately keeping track of the concentrations of parent and daughter nuclides in the solid and the fluid. In this case, assuming steady state, two equations are used to account for the daughter nuclide ... [Pg.213]

Sediment may be added by bulk mixing via imbricate thnisting (Bebout and Barton 2002), dehydration (Class et al. 2000), or melting (Johnson and Plank 1999). The latter two may differ in their P-T conditions and, therefore, residual mineralogy as well as relevant partition coefficients. In general, fluids are less effective transport agents than melts (i.e., trace elements are more soluble in melt than in pure water or even brine), but fluid/solid partitioning can fractionate some elements, notably Ba-Th and U-Th, more than melt/solid. However, as pressure increases, the distinction between fluid and melt decreases as their mutual solubility increases and they approach a critical end-point. [Pg.271]

The Mechanism of Ion Transport in Solutions, Solids, Melts and Polymers... [Pg.131]

The mobility of ions in melts (ionic liquids) has not been clearly elucidated. A very strong, constant electric field results in the ionic motion being affected primarily by short-range forces between ions. It would seem that the ionic motion is affected most strongly either by fluctuations in the liquid density (on a molecular level) as a result of the thermal motion of ions or directly by the formation of cavities in the liquid. Both of these possibilities would allow ion transport in a melt. [Pg.138]

Properties and handling. Adipic add doesn t physically fit the usual image of an acid. Its melting temperature is 306°F. At normal temperatures, it is a white, crystalline powder that can be transported in one-ton cartons and in drums and 50-pound bags. Adipic acid is only slightly soluble in water but dissolves in alcohol. The commercially traded grade is 99-5% pure. [Pg.263]

Because the melting point of sodium metal is about 98° C (a bit lower than the boihng point of water), it is heated into a liquid phase and then transported in rail tank cars, where it cools and solidifies. When it arrives at its destination, heating coils in the tanks warm it back to the liquid stage, and it is then stored for use. Because sodium has a high specific heat rating, a major use is as a liquid coolant for nuclear reactors. Even though sodium (both solid and liquid) is extremely reactive with water, it has proven safe as a coolant for nuclear reactors in submarines. [Pg.52]

Melting of two crystalline phases initially occurs at their contact because the melting point of a pure phase is high and the solidus of two phases is lower (Figure 4-34). After a melt is produced, the melting continues as each mineral melts (or dissolves) into the melt. Depending on the type of systems, the melting may be controlled by mass transport in the melt, interface reaction, or diffusion in the crystalline phase. [Pg.434]


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Melt transport

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