Fly ash benificiation process

Claim 2

The process for the manufacturing of an enhanced pozzolanic material from fly ash comprising the steps of: (1) mixing dry fly ash with water to form a slurry; (2) mixing a frothing agent with the slurry and agitating to form a carbon-rich froth and removing said froth therefrom to leave an essentially carbon free-fraction having less than 1 percent carbon by weight; (3) removing the cenospheres from said carbon-free fraction; (4) subjecting said carbon-free fraction to wet magnetic separation to remove the iron-rich particles therefrom providing a subfraction which is substantially free of magnetic iron; (5) reducing said subfraction in size by wet grinding to fracture the larger elements and increase the surface area thereof; and (6) drying the ground product to provide an enhanced pozzolanic material which is essentially free of carbon and magnetic iron oxide and in which the particle size is finer than said fly ash.

Claim 3

The process of claim 1 including the additional step of adding approximately 5 pounds of lime per ton of the ground product and conditioning to coat the individual particles with lime.

Claim 4

The process of claim 2 in which said lime is added prior to the drying step.

Claim 5

The process of claim 1 comprising the additional step of adding a dispersant to the product.

Claim 6

The process for the modification of raw fly ash comprising the steps of: (1) mixing dry electrostatic fly ash with water to form a slurry; (2) conditioning and adding a frothing agent to said slurry to form a carbon-rich forth; (3) removing said froth therefrom to leave an essentially carbon-free fraction; (4) subjecting said carbon-free fraction to wet magnetic separation to remove a major portion of the magnetic particles; (5) reducing said carbon-free fraction by wet grinding to fracture the larger elements and increase the surface area thereof; and (6) drying the ground product to provide a fine material which is essentially free of carbon and magnetic iron oxide and in which the particle size is finer than said fly ash.

Claim 7

The process for the modification of raw fly ash comprising the steps of: (1) mixing dry electrostatic fly ash with water to form a slurry; (2) conditioning and adding a frothing agent to said slurry to form a carbon-rich forth; (3) removing said froth therefrom to leave an essentially carbon-free fraction; (4) subjecting said carbon-free fraction to wet magnetic separation to remove a major portion of the magnetic particles; (5) reducing said carbon-free fraction by wet grinding to fracture the larger elements and increase the surface area thereof; and (6) drying the ground product to provide a fine material which is essentially free of carbon and magnetic iron oxide and in which the particle size is finer than said fly ash.

Claim 8

The process of claim 5 including the additional step of adding approximately 5 pounds of lime per ton of the ground product and conditioning to coat the individual particles with lime to provide an enhanced pozzolan.

Claim 9

The process for the manufacture of an inert mineral filler or the like from raw fly ash comprising the steps of: (1) mixing dry fly ash with water to form a slurry; (2) conditioning said slurry with kerosene and mixing a frothing agent therewith to form a carbon-rich froth and removing said froth therefrom to leave an essentially carbon-free fraction; (3) subjecting said carbon-free fraction to wet magnetic separation to remove the iron-rich particles therefrom providing a subfraction containing no more than 6 percent magnetic iron; (4) reducing said subfraction in size by wet grinding to fracture the larger elements and increase the surface area thereof; and (5) drying the ground product to provide a finely reduced mineral filler which is essentially free of carbon and iron oxide.

Claim 10

The process for the manufacture of an inert mineral filler or the like from raw fly ash comprising the steps of: (1) mixing dry fly ash with water to form a slurry; (2) conditioning said slurry with kerosene and mixing a frothing agent therewith to form a carbon-rich froth and removing said froth therefrom to leave an essentially carbon-free fraction; (3) subjecting said carbon-free fraction to wet magnetic separation to remove the iron-rich particles therefrom providing a subfraction containing no more than 6 percent magnetic iron; (4) reducing said subfraction in size by wet grinding to fracture the larger elements and increase the surface area thereof; and (5) drying the ground product to provide a finely reduced mineral filler which is essentially free of carbon and iron oxide.

Claim 11

The process for the recovery of a pozzolan, an inert filler, or the like, from raw fly ash comprising the steps of: (1) mixing dry electrostatic fly ash with water to form a slurry of about 65 percent fly ash and 35 percent water; (2) adding kerosene at the rate of approximately 2 pounds per ton of fly ash and conditioning for at least 1/2 hour; (3) adding a frothing agent prior to the conclusion of conditioning to form a carbon-rich froth; (4) removing said froth by flotation to leave an essentially carbon-free residue; (5) removing the cenospheres from said residue by flotation; (6) passing the remaining product through a wet magnetic separator and removing an iron-rich fraction therefrom which comprises approximately 50-80 percent ferric oxide and leaving a remainder which has approximately 6 percent magnetic iron content or less; (7) wet grinding said remainder in a ball mill to reduce particle size so that approximately all thereof will pass a 325 mesh screen; and (8) drying the ground product.

Claim 12

The process for the recovery of a pozzolan, an inert filler, or the like, from raw fly ash comprising the steps of: (1) mixing dry electrostatic fly ash with water to form a slurry of about 65 percent fly ash and 35 percent water; (2) adding kerosene at the rate of approximately 2 pounds per ton of fly ash and conditioning for at least 1/2 hour; (3) adding a frothing agent prior to the conclusion of conditioning to form a carbon-rich froth; (4) removing said froth by flotation to leave an essentially carbon-free residue; (5) removing the cenospheres from said residue by flotation; (6) passing the remaining product through a wet magnetic separator and removing an iron-rich fraction therefrom which comprises approximately 50-80 percent ferric oxide and leaving a remainder which has approximately 6 percent magnetic iron content or less; (7) wet grinding said remainder in a ball mill to reduce particle size so that approximately all thereof will pass a 325 mesh screen; and (8) drying the ground product.

Claim 13

The process useful in the manufacture of an enhanced pozzolanic material from dry electrostatic fly ash comprising the steps of: 1. mixing the dry fly ash with water to form a flowable slurry; 2. conditioning said slurry for at least 1/2 hour in the presence of a flotation agent to separate the carbon-rich particles from said slurry and to form a carbon-free rich froth; 3. removing said froth from said slurry to leave a fly ash product which has less than 1% carbon by weight; 4. subjecting said product to wet magnetic separation to remove the iron-rich particles therefrom; and thereafter 5. reducing said product by wet grinding to fracture the larger particles and to decrease the particle size so that approximately 100% thereof passes a 325 mesh screen by wet analysis.

Claim 14

The process useful in the manufacture of an enhanced pozzolanic material from dry electrostatic fly ash comprising the steps of: 1. mixing the dry fly ash with water to form a flowable slurry; 2. conditioning said slurry for at least 1/2 hour in the presence of a flotation agent to separate the carbon-rich particles from said slurry and to form a carbon-free rich froth; 3. removing said froth from said slurry to leave a fly ash product which has less than 1% carbon by weight; 4. subjecting said product to wet magnetic separation to remove the iron-rich particles therefrom; and thereafter 5. reducing said product by wet grinding to fracture the larger particles and to decrease the particle size so that approximately 100% thereof passes a 325 mesh screen by wet analysis.

Claim 15

An enhanced pozzolan for use as a replacement for Portland cement in cementatious mixtures comprising water conditioned fly ash having less than 1 percent carbon, less than 6 percent magnetic iron, and a size so that about 100 percent thereof passes a 325 mesh screen by wet analysis.

Claim 16

An enhanced pozzolan for use as a replacement for Portland cement in cementatious mixtures comprising water conditioned fly ash having less than 1 percent carbon, less than 6 percent magnetic iron, and a size so that about 100 percent thereof passes a 325 mesh screen by wet analysis.

Claim 17

A siliceous industrial filler consisting of fly ash particles having no more than 1 percent carbon and no more than 6 percent magnetic iron oxide expressed as Fe 2 O 3 by weight, and of a size so that 100 percent passes a 325 mesh screen by wet analysis.

Claim 18

A siliceous industrial filler consisting of fly ash particles having no more than 1 percent carbon and no more than 6 percent magnetic iron oxide expressed as Fe 2 O 3 by weight, and of a size so that 100 percent passes a 325 mesh screen by wet analysis.