Method of recovering waste heat from furnace flue gases using a granular heat exchange means

Claim 3

In a method of melting glass wherein glassmaking ingredients are fed into a melting furnace, air and fuel are directed into the furnace for combustion therein so as to heat and melt the glassmaking ingredients, and an exhaust gas stream is passed from the furnace, the improvement comprising: passing at least a portion of the exhaust gas stream through a bed of granules in a first heat exchange vessel so as to heat the granules and extract heat from the exhaust gas, removing the heated granules from the bed and passing heated granules to a second heat exchange vessel, passing a stream of air into the second heat exchange vessel and into contact with the heated granules so as to heat the air by extracting heat from the granules, and passing the heated air from the second heat exchange vessel to the melting furnace for combustion.

Claim 4

In a method of melting glass wherein glassmaking ingredients are fed into a melting furnace, air and fuel are directed into the furnace for combustion therein so as to heat and melt the glassmaking ingredients, and an exhaust gas stream is passed from the furnace, the improvement comprising: passing at least a portion of the exhaust gas stream through a bed of granules in a first heat exchange vessel so as to heat the granules and extract heat from the exhaust gas, removing the heated granules from the bed and passing heated granules to a second heat exchange vessel, passing a stream of air into the second heat exchange vessel and into contact with the heated granules so as to heat the air by extracting heat from the granules, and passing the heated air from the second heat exchange vessel to the melting furnace for combustion.

Claim 5

The method of claim 1 or 2 wherein the exhaust gas stream passing from the furnace includes particulate materials, and passage of the exhaust gas through the bed of granules in the first heat exchange vessel deposits at least a portion of the particulate material in the bed.

Claim 6

The method of claim 1 or 2 wherein the granular material comprises aggregates of stone, ceramic, glass or metal.

Claim 7

The method of claim 4 wherein the granular material is gravel.

Claim 8

The method of claim 4 wherein the granules are continuously cycled between the first heat exchange vessel and the second heat exchange vessel.

Claim 9

The method of claim 3 wherein an electric field is imposed across the bed of granules in the first heat exchange vessel as the exhaust gas is passed therethrough so as to enhance deposition of particulate materials in the bed.

Claim 10

The method of claim 7 wherein particulates in the exhaust gas are electrically charged prior to passage through the bed.

Claim 11

The method of claim 3 wherein particulates in the exhaust gas are electrically charged prior to passage through the bed.

Claim 12

The method of claim 3 wherein the granules after removal from the first heat exchange vessel and prior to entering the second heat exchange vessel, are substantially separated from particulates deposited thereon.

Claim 13

The method of claim 1 or 2 wherein the bed of granules in the first heat exchange vessel is maintained in an annular configuration through which exhaust gas flows radially.

Claim 14

The method of claim 1 or 2 wherein the heated granules pass through the second heat exchange vessel in an annular configuration through which air flows radially.

Claim 15

The method of claim 1 or 2 wherein the granules are removed from the first heat exchange vessel after their temperature exceeds 200° C.

Claim 16

The method of claim 13 wherein air is maintained in contact with the heated granules in the second heat exchange vessel for a sufficient time to heat the air to at least 200° C.

Claim 17

The method of claim 13 wherein the granules are removed from the first heat exchange vessel when their temperature is at least 300° C.

Claim 18

The method of claim 3 wherein a substantial portion of the particulate materials are removed from the exhaust gas before being passed through the first heat exchange vessel.

Claim 19

The method of claim 16 wherein the particulate removal is effected by passage of the exhaust gas through a granular filter medium before being passed through the first heat exchange vessel.

Claim 20

The method of claim 17 wherein exhaust gas passes through the granular filter medium and the bed of granules within a unitary first heat exchange vessel.

Claim 21

The method of claim 18 wherein the granular filter medium and the bed of granules are contained in concentric, annular configurations.

Claim 22

The method of claim 17 wherein the granular filter medium is cullet, and the cullet is subsequently fed to a glass melting furnace.

Claim 23

The method of claim 1 or 2 wherein the first heat exchange vessel and the second heat exchange vessel are in vertical alignment with one another, and the granules are contained within a continuous annular path as they pass through the first heat exchange vessel and the second heat exchange vessel.

Claim 24

The method of claim 21 wherein the first heat exchange vessel overlies the second heat exchange vessel, and the granules pass from the first heat exchange vessel to the second heat exchange vessel by means of gravity.

Claim 25

The method of claim 21 wherein the second heat exchange vessel overlies the first heat exchange vessel, and the granules pass from the second heat exchange vessel to the first heat exchange vessel by means of gravity.

Claim 26

The method of claim 2 wherein said furnace is adjacent to a second furnace melting glass in the same manner, cullet comprises a portion of the glassmaking ingredients fed to both furnaces, and exhaust gas from the second furnace is brought into contact with the cullet to preheat the cullet before being fed to both furnaces.

Claim 27

The method of claim 24 wherein heated air from the second heat exchange vessel is passed to said furnace and the second furnace.