Glass melting process with very low to zero-co2 emission

Patent metadata

Field	Value
Publication number	US-2025346517-A1
Application number	US-202318871289-A
Country	US
Kind code	A1
Filing date	Jun 19, 2023
Priority date	Jul 6, 2022
Publication date	Nov 13, 2025
Grant date	—

Abstract

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 2 from the flue gas.

First claim

1 : A method for melting vitrifiable materials to produce flat glass, comprising:
providing a furnace comprising:
(i) a melting tank comprising at least an upstream zone covered by a crown C 1 and equipped with an electrical heating means, a downstream zone covered by a crown C 2 and equipped with a combustion heating means, and a transition zone between the crown C 1 and the crown C 2 ,
(ii) a fining tank covered by a crown C 4 and equipped with an oxy-combustion heating means,
(iii) a neck covered by a crown C 3 and separating the melting tank and the fining tank,
(iv) at least one inlet means located at the melting tank,
(v) an outlet means located downstream of the fining tank, and
(vi) at least one extraction means of a flue gas located at the at least one upstream zone,
the furnace having a height H 1 of the crown C 1 defined by: H 1 ≤0.75*H 2 , H 2 being a height of the crown C 2 , L 1 being a length of the at least one upstream zone defined by: 0.25*(L 1 +L 2 )≤L 1 ≤0.8*(L 1 +L 2 ), L 2 being a length of the downstream zone, and LT being a length of the transition zone defined by: LT≤0.2*(L 1 +L 2 );
charging the vitrifiable materials comprising raw materials and cullet in the melting tank with the at least one inlet means, an amount of the cullet being at least 10% in weight of a total amount of the vitrifiable materials;
cullet pre-heating, at least partially by recovering heat from the furnace, before charging the cullet in the melting tank;
melting the vitrifiable materials in the melting tank with the electrical heating means and the combustion heating means;
fining the melt in the fining tank by heating with the oxy-combustion heating means fed with gas and/or hydrogen;
flowing the melt from the fining tank to a working zone through the outlet means; and
capturing CO 2 from the flue gas, the flue gas having a CO 2 concentration of at least 35%;

wherein an electrical input fraction is from 30% to 85% and the capturing of the CO 2 from the flue gas comprises a compression and/or a dehydration.

2 : The method for melting vitrifiable materials according to claim 1 , wherein the amount of the cullet is at least 30% in weight of a total amount of the vitrifiable materials.

3 : The method for melting vitrifiable materials according to claim 1 , wherein the oxy-combustion heating means are fed with at least 50% hydrogen.

4 : The method for melting vitrifiable materials according to claim 1 , wherein the flue gas CO 2 concentration is at least 40%.

5 : The method for melting vitrifiable materials according to claim 4 , wherein the flue gas CO 2 concentration is at least 50%.

6 : The method for melting vitrifiable materials according to claim 1 , wherein the capturing of the CO 2 from the flue gas consists essentially of compression and/or dehydration.

7 : The method for melting vitrifiable materials according to claim 1 , further comprising:
eliminating acidic components from the flue gas.

8 : The method for melting vitrifiable materials according to claim 1 , wherein the eliminating of the acidic components from the flue gas is prior or concurrent to the capturing of the CO 2 .

9 : The method for melting vitrifiable materials according to claim 1 , wherein a maximum temperature of the cullet at the pre-heating of the cullet is 450° C.

10 : The method for melting vitrifiable materials according to claim 1 , further comprising:
pre-melting at least a part of the cullet in an auxiliary melting tank and flowing the pre-melted cullet to the melting tank.

11 : The method for melting vitrifiable materials according to claim 1 , wherein the raw materials comprise less than 25% in weight of carbonate compounds.

12 : The method for melting vitrifiable materials according to claim 1 , wherein the oxy-combustion heating means are fed with at least 80% hydrogen.

Assignees

• Agc Glass Europe

Inventors

• Bioul François
• Symoens Bruno
• Bourgeois Nicolas
• Habibi Zakaria
• Fasilow Fabrice

Classifications

• C03B2211/40

  using oxy-fuel burners · CPC title

• C03B5/26

  Outlets {, e.g. drains, siphons}; Overflows {, e.g. for supplying the float tank, tweels} · CPC title

• C03B5/2353 Primary

  by combustion with pure oxygen or oxygen-enriched air, e.g. using oxy-fuel burners or oxygen lances · CPC title

• C03B5/005

  of glass-forming waste materials (disposal or transformation of solid waste in general B09B; treatment of radioactive waste G21F9/00) · CPC title

• C03B1/00

  Preparing the batches (chemical compositions C03C) · CPC title