Methods and systems for controlling bubble size and bubble decay rate in foamed glass produced by a submerged combustion melter
Methods and systems for controlling bubble size and bubble decay rate of glass foams formed during submerged combustion melting. Flowing a molten mass of foamed glass comprising molten glass and bubbles entrained therein into an apparatus downstream of a submerged combustion melter. The downstream apparatus has a floor, a roof, and a sidewall structure connecting the floor and roof. The foamed glass has glass foam of glass foam bubbles on its top surface, and the downstream apparatus defines a space for a gaseous atmosphere above and in contact with the glass foam. The downstream apparatus includes heating components to heat or maintain temperature of the foamed glass. Adjusting composition of the atmosphere above the glass foam, and/or contacting the foam with a liquid or solid composition controls bubble size of the glass foam bubbles, and/or foam decay rate.
1. A method comprising:
flowing a molten mass of foamed glass comprising molten glass and bubbles entrained therein into an apparatus downstream of a submerged combustion melter, the downstream apparatus comprising a floor, a roof, and a sidewall structure connecting the floor and roof, the foamed glass having glass foam comprising glass foam bubbles on at least a portion of a top surface of the foamed glass, the downstream apparatus defining a space for a gaseous atmosphere above and in contact with the glass foam;
heating or maintaining temperature of the foamed glass in the downstream apparatus; and
controlling bubble size of the glass foam bubbles in the foamed glass by controlling composition of the atmosphere above the glass foam in the downstream apparatus;
wherein the heating or maintaining temperature of the foamed glass in the downstream apparatus is devoid of electrical heating, and comprises using one or more non-submerged oxy-fuel combustion burners positioned in corresponding apertures in the sidewall structure and/or the roof of the downstream apparatus, the non-submerged oxy-fuel combustion burners producing combustion products contributing to control of the atmosphere above the glass foam;
wherein the controlling of the composition of the atmosphere above the glass foam comprises injecting a non-combustion composition into at least a portion of the atmosphere from a source outside of the downstream apparatus using one or more apparatus positioned in one or more apertures in the sidewall structure and/or the roof; and
wherein the non-combustion composition comprises 10 mole percent of an oxygenated sulfur compound or less.
2. The method of claim 1 wherein the non-combustion composition comprises 1 mole percent of the oxygenated sulfur compound or less.
3. A method comprising:
flowing a molten mass of foamed glass comprising molten glass and bubbles entrained therein into an apparatus downstream of a submerged combustion melter, the downstream apparatus comprising a floor, a roof, and a sidewall structure connecting the floor and the roof, the foamed glass having glass foam comprising glass foam bubbles on at least a portion of a top surface of the foamed glass, the downstream apparatus defining a space for a gaseous atmosphere above and in contact with the glass foam;
heating or maintaining temperature of the foamed glass in the downstream apparatus, wherein the heating or maintaining temperature of the foamed glass in the downstream apparatus is devoid of electrical heating, and comprises using one or more non-submerged oxy-fuel combustion burners positioned in corresponding apertures in the sidewall structure and/or the roof of the downstream apparatus, the non-submerged oxy-fuel combustion burners producing combustion products contributing to control of the atmosphere above the glass foam; and
controlling a foam decay rate of the glass foam bubbles by injecting a non-combustion composition into at least a portion of the atmosphere from a source outside of the downstream apparatus using one or more apparatus positioned in one or more apertures the sidewall structure and/or the roof, wherein the non-combustion composition comprises 10 mole percent of an oxygenated sulfur compound or less.
4. The method of claim 3 wherein the non-combustion composition comprises 1 mole percent of the oxygenated sulfur compound or less.