Wet process for fly ash beneficiation

Claim 2

A wet process for fly ash beneficiation comprising the steps of: a) mixing a fly ash material having cenospheres with a dispersant and water to form a primary slurry from about 5 to about 35 percent by weight fly ash material; b) allowing the primary slurry to settle and removing the cenospheres floating in the primary slurry for separating and collecting the cenospheres having a density below about 1.0 g/cc from the primary slurry to form a secondary slurry; c) adding a constituent soluble in the water to form a water solution between 1.0 g/cc and about 1.6 g/cc and allowing particles of the fly ash material with a density between 1.0 g/cc and about 1.6 g/cc to float in the secondary slurry and thereafter removing and collecting these particles from the secondary slurry to form a tertiary slurry; d) separating and collecting magnetic materials from the tertiary slurry by imposing a magnetic field from about 100 gauss to about 10 kilogauss and removing the magnetic materials to form a fourth slurry; e) adding from about 0.5 to about 10 pounds of an oil having a carbon chain greater than octane per ton of fly ash material and a frothing agent to the fourth slurry, whereby the oil will coat remaining unburned carbon in the fourth slurry to form hydrophobic carbon particles; f) introducing air into the fourth slurry to carry the hydrophobic carbon particles to a frothy layer; and g) removing and collecting the hydrophobic carbon particles from the frothy layer; and h) collecting from the carbon depleted slurry the remaining fly ash material by filtering the carbon depleted slurry.

Claim 3

The process of claim 1 wherein step d) further comprises a two part step of first subjecting the tertiary slurry to a high intensity magnetic field from about 1 to about 10 kilogauss for separating both highly magnetic materials and weakly magnetic materials and collecting the highly and weakly magnetic materials and thereafter subjecting the collected highly and weakly magnetic materials to a low intensity magnetic field from about 100 gauss to about 500 gauss for removing and collecting the highly magnetic materials.

Claim 4

The process of claim 1 wherein the constituent of step c) is selected from the group consisting of iodine, bromide, and sulfate salts.

Claim 5

The process of claim 1 wherein step c) is repeated for sequentially separating materials of sequentially increasing densities out of the secondary slurry.

Claim 6

The process of claim 1 wherein the primary slurry of step a) is formed from 10% to 30% by weight fly ash material.

Claim 7

The process of claim 1 wherein the dispersant is added to the primary slurry in a concentration of from about 0.01 to about 4 pounds per ton of fly ash material.

Claim 8

The process of claim 1 wherein the dispersant is selected from the group consisting of silicates, phosphates, polycrylic acids, ligno sulfonates and mixtures thereof.

Claim 9

The process of claim 1 wherein the dispersant is selected from the group consisting of sodium silicates, sodium tripolyphosphate and mixtures thereof.

Claim 10

The process of claim 1 wherein step d) comprises separating a highly magnetic material fraction from the tertiary slurry by subjecting the tertiary slurry to a magnetic field from about 100 to about 500 gauss.

Claim 11

The process of claim 1 wherein step d) comprises separating a highly magnetic material fraction from the tertiary slurry by subjecting the tertiary slurry to a magnetic field from about 200 to about 400 gauss.

Claim 12

The process of claim 1 wherein step d) comprises separating a highly magnetic material fraction from the tertiary slurry by subjecting the tertiary slurry to a magnetic field from about 250 to about 350 gauss.

Claim 13

A wet process for fly ash beneficiation comprising the steps of: a) mixing a primary slurry of a fly ash material having cenospheres with water and a dispersant selected from the group consisting of silicate phosphates, polyacrylic acids, ligno sulfonates and mixtures thereof; b) allowing the primary slurry to settle and removing the cenospheres floating in the primary slurry thereof for separating the cenospheres having a density below about 1.0 g/cc from the primary slurry to form a secondary slurry; c) adding an alkali halide or sulfate salt to said secondary slurry to increase the density of said secondary slurry and subjecting said increased density secondary slurry to gravity flotation which results in the removal of a second fraction of materials having a greater density than said secondary slurry increased density to form a tertiary slurry; d) removing a magnetic fraction of fly ash material by running the tertiary slurry through a magnetic separator at a magnetic field strength of from about 1 to about 5 kilogauss to form a fourth slurry; e) collecting the magnetic fraction from the tertiary slurry and further separating highly magnetic materials from weakly magnetic materials by subjecting the magnetic fraction to a magnetic field from about 100 gauss to about 500 gauss; f) removing unburned carbon from the fourth slurry by: i) adding an effective amount from about 0.5 to about 10 pounds of a collection composition per ton of fly ash material suitable for forming hydrophobic carbon particles in the fourth slurry; ii) adding a frothing agent to the fourth slurry; iii) introducing air into the fourth slurry for frothing the fourth slurry carrying the hydrophobic carbon particles to the surface; and iv) collecting the hydrophobic carbon particles from the fourth slurry to form a fifth slurry; and g) collecting the remaining fraction of fly ash material comprising silicate spheres and other silicates from the fifth slurry.

Claim 14

A wet process for fly ash beneficiation comprising the steps of: a) mixing a primary slurry of a fly ash material having cenospheres with water and a dispersant selected from the group consisting of silicate phosphates, polyacrylic acids, ligno sulfonates and mixtures thereof; b) allowing the primary slurry to settle and removing the cenospheres floating in the primary slurry thereof for separating the cenospheres having a density below about 1.0 g/cc from the primary slurry to form a secondary slurry; c) adding an alkali halide or sulfate salt to said secondary slurry to increase the density of said secondary slurry and subjecting said increased density secondary slurry to gravity flotation which results in the removal of a second fraction of materials having a greater density than said secondary slurry increased density to form a tertiary slurry; d) removing a magnetic fraction of fly ash material by running the tertiary slurry through a magnetic separator at a magnetic field strength of from about 1 to about 5 kilogauss to form a fourth slurry; e) collecting the magnetic fraction from the tertiary slurry and further separating highly magnetic materials from weakly magnetic materials by subjecting the magnetic fraction to a magnetic field from about 100 gauss to about 500 gauss; f) removing unburned carbon from the fourth slurry by: i) adding an effective amount from about 0.5 to about 10 pounds of a collection composition per ton of fly ash material suitable for forming hydrophobic carbon particles in the fourth slurry; ii) adding a frothing agent to the fourth slurry; iii) introducing air into the fourth slurry for frothing the fourth slurry carrying the hydrophobic carbon particles to the surface; and iv) collecting the hydrophobic carbon particles from the fourth slurry to form a fifth slurry; and g) collecting the remaining fraction of fly ash material comprising silicate spheres and other silicates from the fifth slurry.

Claim 15

The process of claim 12 wherein the density of step c) is increased to from about 1.3 to about 1.4.

Claim 16

The process of claim 12 wherein the amount of dispersant added is from about 0.2 to about 2 pound per ton of fly ash material.

Claim 17

The process of claim 14 wherein the dispersant is selected from the group consisting of silicates, phosphates, polycrylic acids, ligno sulfonates and mixtures thereof.

Claim 18

The process of claim 15 wherein the dispersant is selected from the group consisting of sodium silicates, sodium tripolyphosphate and mixtures thereof.

Claim 19

The process of claim 12 wherein the highly magnetic material of step e) is collected by subjecting the magnetic fraction to a magnetic field of from about 200 to 400 gauss.

Claim 20

The process of claim 12 wherein the highly magnetic material of step e) is collected by subjecting the magnetic fraction to a magnetic field of from about 250 to 350 gauss.

Claim 21

The process of claim 12 wherein the collection composition added is the amount from about 0.5 to about 5 pounds per ton of fly ash material.

Claim 22

The process claim 12 wherein the collection composition added is the amount from about 1 to 4 pounds per ton of fly ash material.