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

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Special energy consumption, normalized to 50 percent cullet in the batch <strong>and</strong> primary<br />

energy equivalents, increased on average with 0.8–0.9 percent per year of age for the 123<br />

investigated glass furnaces. This means that during five to 14 years of furnace lifetime,<br />

energy consumption may increase by seven to 10 percent due to refractory wear, which<br />

causes greater wall heat losses, air leakage, insulation wear, or plugging <strong>and</strong> fouling of<br />

regenerators. For large end port regenerative <strong>and</strong> recuperative LoNOx melters with cullet<br />

preheaters that use 70 percent cullet, energy consumption levels were about 3.7–3.8<br />

mmBt/short ton (normalized to 50 percent cullet).<br />

The Sankey diagram (Figure I.3.) of energy flows in the most energy-efficient container<br />

glass furnace—cross-fired regenerative furnace without electric boosting—75 percent<br />

cullet, with batch preheating. About 49 percent of the energy input was used for heating<br />

the glass <strong>and</strong> the fusion reactions. <strong>Glass</strong> melt energy represents sensible heat of the glass<br />

at throat temperature.<br />

Figure I.3. Crossfired regenerative 70-75% cullet <strong>and</strong> batch preheat Sankey diagram from<br />

Ruud Beerkens, TNO; represents one of the 10% most energy efficient furnaces<br />

(container glass) in Europe<br />

The general consensus of European glass manufacturers is that batch preheating can<br />

potentially decrease specific energy consumption by about 10 to 15 percent. By<br />

increasing cullet for raw material by 10 percent, energy input requirements could be<br />

reduced by 2 to 5 percent. As the lining of the furnace deteriorates with age, energy input<br />

requirements can increase by 0.1–0.2 percent per month.<br />

I.3.3. Operating costs for capital productivity<br />

With few new glass plants being built in the US over the past few years <strong>and</strong> additional<br />

production needed to meet market dem<strong>and</strong>, glass manufacturers have attempted to<br />

increase productivity by increasing output from established furnaces. Since space in<br />

most glass plant facilities is limited, the possibilities for expansion of furnace size are<br />

limited, <strong>and</strong> capital cost to build new furnaces is high. Manufacturers may choose to<br />

accept the extra cost of melting per ton of glass by increasing production with electric<br />

boosting of fossil fuel or adapting to oxygen firing.<br />

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