Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
256 words
A process for extracting alumina and cement constituents from fly ash which comprises; a. subjecting the fly ash to magnetic separation by known methods yielding an iron-bearing magnetic fraction and a nonmagnetic fraction, and b. dry mixing the nonmagnetic fraction with a calcining agent, CaO, wherein the ratio of CaO to SiO 2 by weight is between 1.4 and 2.0, and said dry mixing yielding a dry mixture, and c. pelletizing the dry mixture by adding a sufficient amount of water and forming pellets which are approximately spherical, and d. drying and calcining the pellets by subjecting the pellets to a temperature of between 900° C. and 1200° C. for between five and thirty hours and yielding calcined fly ash, and e. acid treating the calcined fly ash, resulting in diluted slurry, and f. selectively increasing the pH of the diluted slurry to 2.0 by the addition of lime, and g. subjecting the diluted slurry to a filtration yielding solids and a pregnant solution, and h. selectively subjecting the pregnant solution to a purification step using an organic solvent, yielding scrub solution and purified pregnant solution, and i. subjecting the purified pregnant solution to evaporation, removing water and seeding the purified pregnant solution with aluminum sulfate crystals, yielding aluminum sulfate suspension, and j. subjecting the aluminum sulfate suspension to a liquid-solid separation which yields a mother liquor and hydrated crystalline aluminum sulfate, and k. calcining the crystalline aluminum sulfate at approximately 1000° C. which drives off the sulfur oxides and water of hydration and yields alumina.
Claim 2
Dependent Claim
256 words
A process for extracting alumina and cement constituents from fly ash which comprises; a. subjecting the fly ash to magnetic separation by known methods yielding an iron-bearing magnetic fraction and a nonmagnetic fraction, and b. dry mixing the nonmagnetic fraction with a calcining agent, CaO, wherein the ratio of CaO to SiO 2 by weight is between 1.4 and 2.0, and said dry mixing yielding a dry mixture, and c. pelletizing the dry mixture by adding a sufficient amount of water and forming pellets which are approximately spherical, and d. drying and calcining the pellets by subjecting the pellets to a temperature of between 900° C. and 1200° C. for between five and thirty hours and yielding calcined fly ash, and e. acid treating the calcined fly ash, resulting in diluted slurry, and f. selectively increasing the pH of the diluted slurry to 2.0 by the addition of lime, and g. subjecting the diluted slurry to a filtration yielding solids and a pregnant solution, and h. selectively subjecting the pregnant solution to a purification step using an organic solvent, yielding scrub solution and purified pregnant solution, and i. subjecting the purified pregnant solution to evaporation, removing water and seeding the purified pregnant solution with aluminum sulfate crystals, yielding aluminum sulfate suspension, and j. subjecting the aluminum sulfate suspension to a liquid-solid separation which yields a mother liquor and hydrated crystalline aluminum sulfate, and k. calcining the crystalline aluminum sulfate at approximately 1000° C. which drives off the sulfur oxides and water of hydration and yields alumina.