A laminate fusion draw apparatus including: a core isopipe having a first core melter; a clad isopipe having a clad melter; a first core down comer between the core melter and the core isopipe; and a second clad down comer between the clad melter and the clad isopipe, the second clad down comer having an independently adjustable linear and horizontal position with respect to a fixed horizontal position of the first down comer, and the core melter and the clad melter are linearly moveable for relative movement in the same or opposite horizontal direction, as described herein. Also disclosed is a method of using the apparatus where the first core down comer remains substantially centered or concentric on the first inlet tube, and the second clad down comer remains substantially centered or concentric on the second inlet tube.

Glass melting furnaces include a melting vessel that includes a floor, a feeding mechanism configured to feed raw materials into the melting vessel, a heating mechanism configured to convert raw materials fed into the melting vessel into molten glass, and a cooling mechanism extending within the floor and configured to flow a cooling fluid therethrough.

Glass melting furnaces include a melting vessel that includes a floor, a feeding mechanism configured to feed raw materials into the melting vessel, a heating mechanism configured to convert raw materials fed into the melting vessel into molten glass, and a cooling mechanism extending within the floor and configured to flow a cooling fluid therethrough.

A method of producing glass includes discharging an outflow (22, 1022) of fined molten glass from a fining tank (18, 1018) of a vacuum induction fining apparatus (10, 1010) and delivering the fined molten glass into a thermal conditioning tank (16, 1016) that is separated from the fining tank by an open space (26, 1026) occupied by an ambient environment (24, 1024). The fining tank includes a vertically-elongated housing (80, 1080) that defines an interior fining chamber (82, 1082) where a bath (76, 1076) of molten glass is collected and maintained. The interior fining chamber is maintained at subatmospheric pressure and the housing is surrounded by at least one induction coil (74, 1074) to introduce heat into the molten glass bath. The vacuum maintained in the interior fining chamber and the heating supplied by the induction coil(s) promote the ascension of gas bubbles upwards through the molten glass bath. A glass-producing system that includes the vacuum induction fining apparatus is also disclosed.

Provided is a glass production method with which oxidation can be suppressed and productivity can be increased. A glass production method according to the present invention includes the steps of: turning a raw material 6 placed in a container 1 into a melt 11; homogenizing the melt 11; removing a gas from the melt 11, wherein at least one of the step of turning the raw material 6 into the melt 11 and the step of homogenizing the melt 11 is performed in an atmosphere of an inert gas or a reducing gas, and in the step of the removing the gas from the melt 11, the inert gas or the reducing gas is removed by setting the temperature of the melt 11 to be lower than the temperature in the step of homogenizing the melt 11.

A method for melting vitrifiable materials to produce flat glass, including: providing a furnace including: a melting tank, a fining tank, a neck, at least one inlet means located at the melting tank, an outlet means located downstream of the fining tank, and at least one extraction means of a flue gas located at the at least one upstream zone; charging the vitrifiable materials including raw materials and cullet in the melting tank with the at least one inlet means; cullet pre-heating; melting the vitrifiable materials in the melting tank; fining the melt in the fining tank; flowing the melt from the fining tank to a working zone through the outlet means; and capturing CO.sub.2 from the flue gas.

A method for melting vitrifiable materials to produce flat glass, including: providing a furnace including: a melting tank, a fining tank, a neck, at least one inlet means located at the melting tank, an outlet means located downstream of the fining tank, and at least one extraction means of a flue gas located at the at least one upstream zone; charging the vitrifiable materials including raw materials and cullet in the melting tank with the at least one inlet means; cullet pre-heating; melting the vitrifiable materials in the melting tank; fining the melt in the fining tank; flowing the melt from the fining tank to a working zone through the outlet means; and capturing CO.sub.2 from the flue gas.

A method of producing glass includes discharging an outflow of fined molten glass from a fining tank of a vacuum induction fining apparatus and delivering the fined molten glass into a thermal conditioning tank that is separated from the fining tank by an open space occupied by an ambient environment. The fining tank includes a vertically-elongated housing that defines an interior fining chamber where a bath of molten glass is collected and maintained. The interior fining chamber is maintained at subatmospheric pressure and the housing is surrounded by at least one induction coil to introduce heat into the molten glass bath. The vacuum maintained in the interior fining chamber and the heating supplied by the induction coil(s) promote the ascension of gas bubbles upwards through the molten glass bath. A glass-producing system that includes the vacuum induction fining apparatus is also disclosed.

A high-strength low-creep overflow brick and a method for designing the same are provided. The method includes: selecting a mature overflow brick for manufacturing a glass substrate as a reference overflow brick, obtaining design parameters of the reference overflow brick, design parameters of a designed overflow brick, and a creep stress exponent of the overflow brick; establishing similarity relationships between the reference and designed overflow bricks, and establishing a system of equations regarding a first height and a second height at an inlet cross-section of the designed overflow brick; determining strength parameters of the reference and designed overflow bricks based on the similarity relationships, the design parameters of the reference and designed overflow bricks, the system of equations; determining a support surface length of the designed overflow brick and a maximum cylinder pressure of a clamp cylinder based on the strength parameters of the reference and designed overflow bricks.