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Glass Melting Technology: A Technical and Economic ... - OSTI

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The presence of some distinct solid particles at high temperatures is beneficial. Since the<br />

solubility of gases decreases as silica content increases, solid s<strong>and</strong> grains provide sites for<br />

nucleation of gas bubbles <strong>and</strong> set up localized convective flow. Also, for efficient<br />

diffusion <strong>and</strong> convection melting reactions <strong>and</strong> destabilization of foam conditions, it is<br />

desirable that the viscosity of the intermediate liquid material phases be as low as<br />

possible. This is achieved by delaying the complete dissolution of silica grains until all<br />

other processes except refining are finished.<br />

Chemical homogenization<br />

<strong>Glass</strong>-forming melt is either present from the beginning in the form of cullet added as a<br />

batch component or is generated when or as the early borate, borosilicate or silicate<br />

eutectic melts. This high-viscosity melt slows down melting reactions, which continue<br />

via diffusion. Melt homogenization proceeds mainly through the growth <strong>and</strong> motion of<br />

bubbles, whether in the batch blanket or during fining. The viscous glass-forming melt<br />

traps gases; large numbers of growing bubbles tend to exp<strong>and</strong> the reacting mixture into<br />

foam (so-called primary foam). Bubbles stretch the membranes of the viscous melt until<br />

they burst <strong>and</strong> shrink back. This is an efficient homogenization mechanism.<br />

Both homogenization <strong>and</strong> segregation occur within the batch blanket. Low-viscosity<br />

molten salts can drain through open pores between refractory particles, enriching the<br />

lower layers of batch with fluxes. However, in a steady state, local enrichments do not<br />

affect the homogeneity of the final product. An example of local enrichment is refluxing.<br />

For example, SOx from deeper <strong>and</strong> hotter layers of the batch condenses in the colder<br />

upper layers, where SOx turns into sodium salts that drain down to be partly absorbed in<br />

the glass <strong>and</strong> partly decomposed. This is particularly true for cold-top electric melters.<br />

Batch segregation can lead to different glass compositions. Only minor levels of<br />

demixing can be overcome via homogenizing mechanisms in the glass fusion process.<br />

When recycled cullet has a different composition than the target glass composition, it is<br />

necessary to rely upon a variety of homogenization mechanisms to obtain a chemically<br />

consistent final glass.<br />

Convection currents within the bulk melt generally operate on a larger scale than bubbles<br />

in batch piles. For these currents to be effective, high velocity gradients are necessary.<br />

These gradients stretch <strong>and</strong> thin melt inhomogeneities, thus helping their attenuation by<br />

diffusion. However, high-viscosity inclusions (such as alumina-rich inhomogeneities)<br />

should be avoided because high-viscosity inhomogeneities are difficult to stretch <strong>and</strong> the<br />

diffusion coefficients of their components are small. Some compositions rely upon<br />

bubblers in the melter to accentuate mixing <strong>and</strong> assimilation of inhomogeneities.<br />

The batch pile, or the cold mixture of raw materials, is melted not only at the surface, but<br />

also from the underside by the molten glass bath. Relatively cold, bubbly glass forms<br />

below the bottom layer of batch material <strong>and</strong> sinks to the bottom of the tank. Appropriate<br />

convection currents must bring this material to the surface, since fining occurs in tank<br />

furnaces primarily at the surface of the melt, where bubbles need to rise only a short<br />

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