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

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silica s<strong>and</strong> with a variety of industrial minerals to produce a particular glass. The industry<br />

segments share common concerns: purchase of batch materials, purchase of energy, <strong>and</strong><br />

melting of batch <strong>and</strong> cullet.<br />

Moreover, they are concerned about such issues as environmental compliance <strong>and</strong><br />

delivery of high-quality glass to downstream operations. Other areas of common interest<br />

include oxygen combustion; electric boosting; bubbling; <strong>and</strong> batch preheating. Each<br />

segment faces different challenges to comply with governmental regulations.<br />

Environmental concerns of segments<br />

Some technologies are better than others in their degree of environmental pollution. The<br />

melting process within combustion-based melters inherently pollutes the environment<br />

with NOx, SOx, <strong>and</strong> particulate emissions. Cold-top electric melters do not emit these<br />

pollutants. However, the higher temperatures of electric melters lead to shorter furnace<br />

life, <strong>and</strong> cost of electric power is higher than that of fossil fuels. Conventional furnaces<br />

have faced ever-increasing requirements for reduced air emissions. Particulate matter<br />

from batch volatile components, i.e., SOx, alkali or borates, all require some level of<br />

control under regional, state <strong>and</strong> federal regulations. All add-on devices require high<br />

capital <strong>and</strong> operating costs but do not improve productivity. Many factories have space<br />

restrictions that prevent add-on options. Regenerative furnace designs with chromebearing<br />

refractories may need to be adapted due to more restrictive waste disposal<br />

regulations.<br />

Alternative technologies must be compared with conventional furnaces based on all<br />

configurations that meet emission control requirements. Particulate control involves a<br />

variety of process modifications, batch adjustments, or add-on devices such as bag houses<br />

or electrostatic precipitators. Adjustments to sulfur-containing batch components or addon<br />

wet or dry scrubbers are needed to control SOx from low-sulfur fuels. Modifications<br />

to the combustion process, changing temperatures <strong>and</strong> reaction possibilities, <strong>and</strong> postcombustion<br />

gas treatment revert NOx back to N2.<br />

Emissions from a glass furnace fired with fossil fuels take the form of combustion<br />

products, namely oxides of sulfur, thermal NOx, <strong>and</strong> carbon dioxide. Other emissions<br />

arise from particulate carryover <strong>and</strong> decomposition of batch materials, particularly CO2<br />

from carbonates, NOx from nitrates, <strong>and</strong> SOx from sulfates. Sulfate is required in<br />

modest levels as a refining agent as well as to promote oxidizing reaction. Emissions<br />

from low level halides or metals <strong>and</strong> fluoride formulations may also occur where these<br />

raw materials are present in a batch.<br />

Emissions of all volatile batch components are considerably lower in electric furnaces<br />

than in conventional furnaces due to the reduced gas flow <strong>and</strong> absorption, condensation,<br />

<strong>and</strong> reaction of gaseous emissions <strong>and</strong> the heat from the melt. However, electric melting<br />

is not currently in use in the US for large volume glass production (>300 tpd). Production<br />

of continuous filament E-glass using 100 percent electric melting is not considered<br />

economically or technically viable. Higher alkali insulating wool fiberglass can be<br />

produced in cold-top all-electric furnaces, up to 200 tpd. A number of these furnaces<br />

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