Process for the calcination and manufacture of synthetic pozzolan
US-9458059-B2 · Oct 4, 2016 · US
US10294152B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10294152-B2 |
| Application number | US-201415101572-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 4, 2014 |
| Priority date | Dec 4, 2013 |
| Publication date | May 21, 2019 |
| Grant date | May 21, 2019 |
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Methods for producing pozzolanic or latent hydraulic cement clinker substitutes may involve calcining clay with a fuel comprising a mineral substance at temperatures in the range from 500 to 1250° C., preferably from 550 to 1150° C., most preferably from 700 to 900° C. A resulting mixture of mineral substance from the fuel and the calcined clay forms a pozzolanic or latent hydraulic cement clinker substitute, in which a fraction of the mineral substance incorporated into the pozzolanic or latent hydraulic cement clinker substitute by the fuel is 1-60% by weight.
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What is claimed is: 1. A method for producing a pozzolanic or latent-hydraulic cement clinker substitute, the method comprising calcining clay at temperatures of between 500 to 1250 degrees Celsius with a fuel comprising a mineral substance, wherein a resulting mixture of the mineral substance from the fuel and the calcined clay forms the pozzolanic or latent-hydraulic cement clinker substitute that includes 1-60% by weight of the mineral substance, wherein the fuel comprising the mineral substance has a ratio of Al 2 O 3 to SiO 2 of 0.13-1.4% by weight and a CaO content of less than 80% by weight. 2. The method of claim 1 wherein the resulting mixture of the mineral substance from the fuel and the calcined clay forms the pozzolanic or latent-hydraulic cement clinker substitute that includes 20-40% by weight of the mineral substance. 3. The method of claim 1 further comprising adjusting properties of the pozzolanic or latent-hydraulic cement clinker substitute via at least one of a particle size distribution of the fuel used for calcining or a composition of the mineral substance contained in the fuel. 4. The method of claim 1 further comprising adjusting a workability of the pozzolanic or latent-hydraulic cement clinker substitute by comminuting the fuel. 5. The method of claim 1 further comprising regulating a chemical composition of the mineral substance resulting from the calcining by using a mixture of fuels having different mineral substance compositions. 6. The method of claim 1 wherein the calcining is performed in a suspension heat exchanger, a rotary kiln, a fluidized bed, or a multitier furnace. 7. The method of claim 1 wherein the fuel is a flyash having a carbon fraction of at least 0.5% by weight. 8. The method of claim 1 further comprising comminuting the clay to particle sizes of less than 10 mm before the calcining. 9. The method of claim 1 further comprising calculating a fraction of the mineral substance supplied to the calcining so as to cause the pozzolanic or latent-hydraulic cement clinker substitute to have a mixing ratio of the calcined clay to the mineral substance of between 0.5:1 to 20:1. 10. The method of claim 1 wherein the fuel has a particle size of between 0.05 to 1 mm. 11. The method of claim 10 wherein the fuel is coal. 12. A method for producing a pozzolanic or latent-hydraulic cement clinker substitute, the method comprising: calcining clay at temperatures of between 500 to 1250 degrees Celsius with a fuel comprising a mineral substance, wherein a resulting mixture of the mineral substance from the fuel and the calcined clay forms the pozzolanic or latent-hydraulic cement clinker substitute that includes 1-60% by weight of the mineral substance; and supplying a flyash to the calcining of the clay and the fuel with the mineral substance. 13. The method of claim 12 wherein the fuel is a flyash having a carbon fraction of at least 0.5% by weight. 14. The method of claim 12 further comprising comminuting the clay to particle sizes of less than 10 mm before the calcining. 15. The method of claim 12 further comprising calculating a fraction of the mineral substance supplied to the calcining so as to cause the pozzolanic or latent-hydraulic cement clinker substitute to have a mixing ratio of the calcined clay to the mineral substance of between 0.5:1 to 20:1. 16. The method of claim 12 wherein the fuel is coal. 17. A method for producing a pozzolanic or latent-hydraulic cement clinker substitute, the method comprising calcining clay at temperatures of between 500 to 1250 degrees Celsius with a fuel comprising a mineral substance, wherein a resulting mixture of the mineral substance from the fuel and the calcined clay forms the pozzolanic or latent-hydraulic cement clinker substitute that includes 1-60% by weight of the mineral substance, wherein the fuel used in the calcining is supplemented with a fuel with a flyash having a carbon fraction of at least 0.5% by weight. 18. The method of claim 17 wherein the calcining is performed in a suspension heat exchanger, a rotary kiln, a fluidized bed, or a multitier furnace. 19. The method of claim 17 wherein the fuel is a flyash having a carbon fraction of at least 0.5% by weight. 20. The method of claim 17 further comprising calculating a fraction of the mineral substance supplied to the calcining so as to cause the pozzolanic or latent-hydraulic cement clinker substitute to have a mixing ratio of the calcined clay to the mineral substance of between 0.5:1 to 20:1.
Carbon capture and storage [CCS] · CPC title
from raw materials containing flue dust {, i.e. fly ash (C04B7/243 takes precedence)} · CPC title
Natural pozzuolanas; Natural pozzuolana cements; {Artificial pozzuolanas or artificial pozzuolana cements other than those obtained from waste or combustion residues, e.g. burned clay; Treating inorganic materials to improve their pozzuolanic characteristics (cements containing slag C04B7/14)} · CPC title
from combustion residues, {e.g. ashes or slags from waste incineration}({C04B7/243} , C04B7/26 take precedence) · CPC title
Cross-Sectional Technologies · mapped topic
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