Molten glass refining apparatus

Claim 2

The improvement in an apparatus for refining glass comprising: (a) an elongated continuous flow refining channel in which a molten vitreous mass is introduced at one end thereof and flowed horizontally therethrough to an exit at its other end; (b) a localized foaming zone extending along a predetermined length of said channel and spaced from the one end thereof, said foaming zone having a width appreciably wider than the channel upstream of said foaming zone; and (c) heating means submerged along the length of said channel for subjecting the flowing molten mass in said foaming zone to an expansion of at least 50% of its initial molten volume by foaming the flowing molten mass in said foaming zone throughout its entire volume as the mass moves along the channel from its one end to the other end.

Claim 3

The apparatus according to claim 1 wherein: (a) the width of the channel in said foaming zone is about twice the width of the channel upstream thereof.

Claim 4

The apparatus according to claim 2 wherein: (a) the width of the channel downstream of the foaming zone is about equal to the width upstream of the foaming zone.

Claim 5

The apparatus according to claim 3 wherein: (a) the length of the channel is about eight times the width of the channel upstream and downstream of the foaming zone; and (b) the length of the foaming zone is about twice that of the channel upstream thereof.

Claim 6

The apparatus according to claim 2 wherein the improvement further includes: (a) a plurality of pairs of electrodes positioned in opposed relation along opposite sides of the channel in submerged relation to the molten mass.

Claim 7

The apparatus according to claim 5 wherein: (a) the electrodes have a heating capacity sufficient to increase the temperature of the molten mass by at least 20° C. per minute.

Claim 8

The apparatus according to claim 5 wherein: (a) the opposed electrodes of each pair extend parallel to each other and to the sides of the channel in spaced relation thereto; and (b) the spacing between the electrodes in the foaming zone is at least equal to the width of the channel upstream of the foaming zone.

Claim 9

The apparatus according to claim 7 wherein: (a) the electrodes extend horizontally near the bottom of the channel; and (b) a single pair of electrodes is disposed in said foaming zone and extends substantially the length of the foaming zone.

Claim 10

The apparatus according to claim 8 wherein: (a) the spacing of the electrodes from the sides of the channel is greater in the foaming zone than along the remainder of the channel.

Claim 11

The apparatus according to claim 8 wherein: (a) the spacing of the electrodes in the foaming zone is about equal to the width of the channel upstream of the foaming zone.

Claim 12

The apparatus according to claim 10 wherein: (a) the width of the channel downstream of the foaming zone is equal to the width upstream of the foaming zone; (b) the length of the channel is about eight times the width of the channel upstream and downstreamm of the foaming zone; and (c) the length of the foaming zone is about twice that of the channel upstream thereof.

Claim 13

The apparatus according to claim 11 wherein: (a) the sides of the channel are more moderately insulated in the foaming zone than upstream and downstream thereof.

Claim 14

In an apparatus for rapidly refining glass of the type having an elongated continuous channel in which a molten vitreous mass is introduced at one end thereof, flowed horizontally therethrough and subjected to an expansion of at least 50% of its initial molten volume by foaming the molten mass throughout its entire volume as the mass moves along the channel from its one end to the other end, the improvement comprising: (a) a plurality of pairs of submerged electrodes horizontally positioned throughout the length of the channel is opposed relation along opposite sides of the channel and adjacent the bottom thereof.

Claim 15

In an apparatus for rapidly refining glass of the type having an elongated continuous channel in which a molten vitreous mass is introduced at one end thereof, flowed horizontally therethrough and subjected to an expansion of at least 50% of its initial molten volume by foaming the molten mass throughout its entire volume as the mass moves along the channel from its one end to the other end, the improvement comprising: (a) a plurality of pairs of submerged electrodes horizontally positioned throughout the length of the channel is opposed relation along opposite sides of the channel and adjacent the bottom thereof.

Claim 16

The improvement in an apparatus for refining glass comprising: (a) an elongated continuous flow refining channel in which a molten vitreous mass is introduced at one end thereof and flowed horizontally therethrough to an exit at its other end; (b) a localized foaming zone extending along a predetermined length of said channel adjacent said one end thereof; (c) first heating means disposed longitudinally along said channel in said foaming zone at a location spaced from the sides and bottom of said channel and below the surface of said vitreous mass for rapidly heating the flowing vitreous mass to cause its entire volume to pass totally to the foam state while in said foaming zone; (d) second heating means disposed longitudinally along the remainder of the channel longitudinally of said foaming zone for heating the flowing vitreous mass; and (e) said first and second heating means being positioned relative to the sides and bottom of said channel and of a sufficient power to generate sufficient heat and produce active transverse thermal convection in said flowing vitreous mass along said channel preventing longitudinal currents tending to mix the vitreous mass of one area of said channel with that of another.

Claim 17

The improvement in an apparatus for refining glass comprising: (a) an elongated continuous flow refining channel in which a molten vitreous mass is introduced at one end thereof and flowed horizontally therethrough to an exit at its other end; (b) a localized foaming zone extending along a predetermined length of said channel adjacent said one end thereof; (c) first heating means disposed longitudinally along said channel in said foaming zone at a location spaced from the sides and bottom of said channel and below the surface of said vitreous mass for rapidly heating the flowing vitreous mass to cause its entire volume to pass totally to the foam state while in said foaming zone; (d) second heating means disposed longitudinally along the remainder of the channel longitudinally of said foaming zone for heating the flowing vitreous mass; and (e) said first and second heating means being positioned relative to the sides and bottom of said channel and of a sufficient power to generate sufficient heat and produce active transverse thermal convection in said flowing vitreous mass along said channel preventing longitudinal currents tending to mix the vitreous mass of one area of said channel with that of another.

Claim 18

The improvement in the apparatus of claim 14 wherein: (a) said first and second heating means comprise electrodes spaced from the sides and bottom of said channel and positioned below the surface of said vitreous material.

Claim 19

The improvement in the apparatus of claim 15 wherein: (a) the electrodes have a heating capacity sufficient to increase the temperature of the molten mass by at least 20° C. per minute.

Claim 20

The improvement in the apparatus of claim 16 wherein: (a) the width of the channel in said foaming zone is appreciably wider than the width of the channel downstream of said foaming zone.