Rotary batch preheater
View Patent ↗Rotary heat-exchanger for glass batch and/or cullet, comprising a stationary casing having a gas inlet and outlet, and an interior region between the gas inlet and outlet; a chamber positioned in the casing rotatable with respect to the casing and configured to receive batch material or a mixture with cullet; at least one heat exchange tube in the casing in fluid communication with the gas inlet and outlet; a feeder in communication with the chamber and comprising a feeder housing configured to discharge the batch material or mixture of batch material and cullet into the chamber along an infeed length and in contact with the at least one tube; wherein the infeed length is a length effective to heat the batch or mixture with cullet material up to at least 100° C. in the infeed length. A method of preheating glass batch is also disclosed.
1 . A rotary heat-exchanger for preheating wet batch material or a wet mixture of batch and cullet material, comprising:
a. a gas inlet annular chamber, a gas outlet annular chamber spaced from said gas inlet annular chamber, and a region between said gas inlet annular chamber and said gas outlet annular chamber;
b. a rotatable chamber positioned in said region and configured to receive batch material or a mixture of batch and cullet material, said rotatable chamber comprising an infeed length and a downstream zone downstream of said infeed length;
c. at least one heat exchange tube in said rotatable chamber in fluid communication with said gas inlet annular chamber and said gas outlet annular chamber, said at least one heat exchange tube having a first end and a second end spaced from said first end;
d. a first tube plate attached to said first end of said at least one tube and a second tube plate attached to said second end of said at least one tube, and an outlet attached to said second tube plate and in communication with said rotatable chamber and downstream of said downstream zone for discharging dry batch material or dry mixture of batch and cullet material;
e. an inlet cylinder extending through said gas outlet annular chamber and attached to said first tube plate, said inlet cylinder being rotatable with said rotatable chamber;
f. a feeder positioned in said inlet cylinder and in communication with said rotatable chamber, said feeder comprising a feeder housing having a bottom and including a slot discharge port in said bottom and an open end discharge port and configured to discharge said wet batch material or wet mixture of batch material and cullet through both said slot discharge port and through said end discharge port into said rotatable chamber along said infeed length and in contact with said at least one tube;
wherein said infeed length is a length effective to heat said wet batch material or mixture of wet batch and cullet material discharged from said feeder housing up to at least 100° C. in said infeed length and evaporate water therefrom.
2 . The rotary heat-exchanger of claim 1 , wherein said feeder comprises a screw auger.
3 . The rotary heat-exchanger of claim 1 , wherein said feeder comprises a driving force for dispersing said batch material or mixture of batch material and cullet into said chamber along said infeed length.
4 . The rotary-heat exchanger of claim 3 , wherein of said driving force comprises a source compressed air.
5 . The rotary heat-exchanger of claim 1 , wherein said feeder housing is configured to discharge said batch material or mixture of batch material and cullet into said rotatable chamber at a rate R (kg/hr) and along said infeed length and in contact with said at least one tube;
wherein said rotatable heat exchanger is configured to transfer heat to said batch material or mixture of batch and cullet material in said rotatable heat exchanger at a rate Q t (kW/m) along said chamber length; and
wherein said infeed length is at least 0.039 R/Q t .
6 . The rotary heat-exchanger of claim 1 , wherein said outlet comprises an outlet cylinder extending through said gas inlet annular chamber.