Methods and systems for controlling carbon burn out
Systems and methods for beneficiating a recovered fly ash material and/or recovering fly ash from an impound site are described. The method may include thermally treating a first portion of a recovered fly ash material to form a thermally treated fly ash having a first temperature of at least 1000° F., and contacting the thermally treated fly ash with a second portion of the recovered fly ash material to cool the thermally treated fly ash to a second temperature of less than or equal to 500° F. and form a fly ash product. The fly ash product may have a carbon content less than 8% by weight, based on the total dry weight of the fly ash product.
1. A system for forming a fly ash-containing product, the system comprising:
a first stage configured for thermally treating a first portion of a fly ash-containing mixture to form a thermally treated mixture; and
a second stage configured for cooling the thermally treated mixture utilizing a second portion of the fly ash-containing mixture to form the fly ash-containing product, wherein the fly ash-containing product is of lower carbon content than the fly ash-containing mixture, based on a total dry weight of the fly ash-containing product;
wherein the system is configured to first separate the fly ash-containing mixture into the first portion and the second portion upstream of the first stage.
2. The system of claim 1 , wherein the first stage involves a combustion chamber configured to expose the first portion of the fly ash-containing mixture to a temperature of at least 1,000° F.
3. The system of claim 1 , wherein in the first stage, the first portion of the fly ash-containing mixture is exposed to a temperature of at least 1,000° F.
4. The system of claim 1 , wherein in the first stage, the first portion of the fly ash-containing mixture is exposed to a temperature in the range of 1,000-1,300° F.
5. The system of claim 1 , wherein the second stage involves a mixing chamber configured to mix the thermally treated mixture with the second portion of the fly ash-containing mixture.
6. The system of claim 5 , wherein the mixing chamber involves at least one of: a ribbon mixer; and a rotating drum.
7. The system of claim 1 , wherein in the second stage, the thermally treated mixture is cooled to a temperature of 500° F. or less.
8. The system of claim 1 , wherein in the second stage, the thermally treated mixture is cooled to a temperature in the range of 200-500° F.
9. The system of claim 1 , wherein the fly ash-containing product is in accordance with ASTM C618 standards, having a loss on ignition (LOI) in the range of 2-6%.