Method and system for heat recovery in an oxy-fuel fired glass furnace
Processes and systems for glass making can utilize heat recovery to improve operational efficiency and flexibility of operation to provide improved yield, higher quality, or more consistent quality glass, and/or other efficiencies. Some embodiments can utilize adjustments in burner operation to account for different manufacturing conditions to provide improved quality of fabricated glass to provide improved yields of glass with a more efficient utilization of heat, which can improve the environmental impact associated with the manufacturing process in addition to improving the operational efficiency and flexibility of the glass manufacturing process.
1 . A method for producing glass comprising:
feeding fuel and oxidant to burners of a furnace to combust the fuel to heat glass making material for making glass such that:
(i) at least one burner in at least one upstream zone of the furnace operates in a mode of operation in which an inner flow of fuel and an inner flow of oxidant are output into the furnace between an upper oxidant conduit and a lower oxidant conduit such that a flame is formed to project into a combustion chamber of the furnace without upper oxidant staging via the upper oxidant conduit and without lower oxidant staging via the lower oxidant conduit while the oxidant is below a pre-selected hot oxidant temperature threshold; and
(ii) at least one burner in at least one downstream zone of the furnace that is downstream of the at least one upstream zone of the furnace is operated in a foam control mode of operation in which an upper oxidant flow is passed out of an upper oxidant conduit of the burner along with an inner flow of fuel and an inner flow of oxidant that are output into the furnace so that combustion of the fuel from the at least one burner in the at least one downstream zone of the furnace forms a flame that extends upwardly to provide a reducing atmosphere adjacent the glass making material in the at least one downstream zone of furnace to dissolve foam back into the glass making material while the oxidant is below the pre-selected hot oxidant temperature threshold.
2 . The method of claim 1 , comprising:
passing flue gas output from the furnace through an oxidant preheater positioned downstream of the furnace between a stack and the furnace; and
preheating at least a portion of the oxidant before the oxidant is fed to the burners of the furnace.
3 . The method of claim 2 , comprising:
detecting a temperature of the oxidant;
in response to detecting the oxidant is at a pre-selected hot oxidant temperature threshold, adjusting operation of the at least one burner in the at least one upstream zone of the furnace so that the at least one burner of the at least one upstream zone of the furnace is adjusted to a mode of operation in which the flame has a radiative underside that is promoted via an oxidant flow passed out of the lower oxidant conduit without oxidant staging being provided via the upper oxidant conduit of the at least one burner of the at least one upstream zone.
4 . The method of claim 3 , wherein the flame has a radiative underside such that radiative heat is directed along an unobstructed radiative path directly to an upper surface of the glass making material in the at least one upstream zone of the furnace.
5 . The method of claim 1 , comprising:
detecting a temperature of the furnace;
in response to detecting the furnace is at a pre-selected hot furnace temperature, adjusting operation of the at least one burner in the at least one upstream zone of the furnace so that the at least one burner of the at least one upstream zone of the furnace is adjusted to a mode of operation in which the flame has a radiative underside that is promoted via an oxidant flow passed out of the lower oxidant conduit without oxidant staging being provided via the upper oxidant conduit of the at least one burner of the at least one upstream zone;
preheating at least a portion of the oxidant via an oxidant preheater positioned to heat the oxidant before the oxidant is fed to the burners of the furnace via flue gas output from the furnace that is passed through the oxidant preheater; and
preheating at least a portion of the fuel via a fuel preheater positioned to heat the fuel before the fuel is fed to the burners of the furnace via flue gas output from the furnace that is passed through the fuel preheater.
6 . The method of claim 5 , comprising:
passing the flue gas output from the furnace to a fluid heater to heat a heating medium that is feedable to a glass making feed material pre-heating device;
feeding a portion of the glass making material to the glass making feed material pre-heating device for preheating the portion of the glass making material;
outputting the preheated portion of the glass making material from the glass making feed material pre-heating device to feed to the furnace.
7 . The method of claim 6 , wherein the glass making feed material pre-heating device includes a rotatable shaft having flights that are rotatable to pass the portion of the glass making material fed to the glass making feed material pre-heating device through the glass making feed material pre-heating device.
8 . The method of claim 6 , comprising:
passing heated air through a hollow shaft of the glass making feed material pre-heating device for passing into the portion of the glass making material as it passes through the glass making feed material pre-heating device.
9 . The method of claim 8 , comprising:
forming a slip stream of the heating medium output from the fluid heater to pass through a heat exchanger for heating the air to output the heated air for feeding to the hollow shaft of the glass making feed material pre-heating device.
10 . The method of claim 1 , comprising:
raising a temperature of the oxidant to a value at or above the pre-selected hot oxidant temperature threshold;
after the oxidant is at or above the pre-selected hot oxidant temperature threshold, adjusting a flow of the oxidant so at least some of the oxidant bypasses an oxidant preheater positioned between the furnace and a stack; and/or
after the oxidant is at or above the pre-selected hot oxidant temperature threshold, adjusting a flow of the fuel so at least some of the fuel bypasses a fuel preheater positioned between the furnace and the stack; and/or
after the oxidant is at or above the pre-selected hot oxidant temperature threshold, adjusting a flow of the flue gas so that at least a portion of the flue gas bypasses the oxidant preheater and/or the fuel preheater.