Method of enhancing the latent hydraulic and/or pozzolanic reactivity of materials
The present invention relates to a method of enhancing the latent hydraulic and/or pozzolanic reactivity of materials, especially of waste and by-products, comprising the steps: providing a starting material containing sources for CaO and at least one of SiO 2 and AI 2 O 3 mixing the starting material with water at a water/solids ratio from 0.1 to 100 hydrothermal treating of the starting material mixed with water in an autoclave at a temperature of 100 to 300° C. and a residence time from 0.1 to 24 hours to provide an autoclaved product suitable as supplementary cementitious material.
1. A method of enhancing the latent hydraulic and/or pozzolanic reactivity of a material comprising the steps:
providing a starting material containing sources for CaO and at least one of SiO 2 and Al 2 O 3 ,
mixing the starting material with water at a water/solids ratio from 0.1 to 100,
hydrothermal treating of the starting material mixed with water in an autoclave at a temperature of 100 to 300° C. and a residence time from 0.1 to 50 hours to provide an autoclaved product with hydraulic, pozzolanic, or latent hydraulic reactivity, and
grinding the autoclaved product to a fineness of 2,000 to 10,000 cm 2 /g.
2. The method according to claim 1 , wherein the starting material has a molar ratio Ca/(Si+Al+Fe) from 1.5 to 3.
3. The method according to claim 2 , wherein the required ratio Ca/(Si+Al+Fe) is adjusted by adding further reactants before treatment begins.
4. The method according to claim 1 , wherein the starting material is selected from the group consisting of high calcium fly ash (calcium content of Class C fly ash), low calcium fly ash (calcium content of Class F fly ash), incineration ash from combustion of municipal wastes both solid and liquid, bottom ash, slag, quartz, sand, gravel, used concrete, asbestos, and mixtures thereof.
5. The method according to claim 1 , further comprising mechanically treating the starting material to optimize particle size and particle size distribution.
6. The method according to claim 1 , wherein further elements or oxides are added in an amount of 0.1 to 30% by weight while mixing the starting materials or in a subsequent step.
7. The method according to claim 6 , wherein the further elements are selected from the group consisting of CaSO 4 ⋅ ½ H 2 O, CaSO 4 , CaHPP 2 ⋅ 2 H 2 O, Ca 3 P 2 O 8 , NaOH, KOH, Na 2 CO 3 , K 2 CO 3 , MgCO 3 ,MgSO 4 , Na 2 Al 2 O 4 , Na 3 PO 4, K 3 PO 4, Na 2 [B 4 O 5 (OH) 4 ] 108 8 H 2 O, CaCl 2 , Ca(NO 3 ) 2 , MgCl 2 , Mg(NO 3 ) 2 , AlCl 3 , Al(NO 3 ) 3 , FeCl 3 , Fe(NO 3 ) 3 , Ca(CH 3 COO) 2 , Mg(CH 3 COO) 2 , Al(CH 3 COO) 3 , Ca(HCOO) 2 , Mg(HCOO) 2 , Al(HCOO) 3 , and mixtures thereof.
8. The method according to claim 1 , wherein the starting material mixture is seeded with seed crystals which contain calcium silicate hydrate, Portland clinker, granulated blast furnace slag, magnesium silicates, calcium sulphate aluminate (belite) cement, sodium silicate, and/or glass powder.
9. The method according to claim 1 , wherein hydrothermal treatment in the autoclave is carried out at a temperature from 150 to 250° C.
10. The method according to claim 1 , wherein the starting material has a molar ratio Ca/(Si+Al+Fe) from 1.5 to 2.5.
11. The method according to claim 1 , wherein hydrothermal treatment in the autoclave is carried out for 16 to 32 hours.
12. The method according to claim 1 , where hydrothermal treatment in the autoclave is carried out for 10 to 40 hours.
13. The method according to claim 1 , wherein the autoclaved product has enhanced hydraulic, pozzolanic, or latent hydraulic reactivity as compared to the starting material.
14. A method of enhancing the latent hydraulic or pozzolanic reactivity of a material, comprising the steps:
providing a starting material containing sources of CaO and at least one of SiO 2 and Al 2 O 3 ,
mixing the starting material with water at a water/solids ratio from 0.1 to 100,
hydrothermal treating of the starting material mixed with water in an autoclave at a temperature of 100 to 300 ° C. and a residence time from 0.1 to 50 hours to provide an autoclaved product,
tempering the autoclaved product at a temperature ranging from 350 to 600 ° C. to provide an autoclaved product with pozzolanic or latent hydraulic reactivity, and
grinding the autoclaved and tempered product to a fineness of 2,000 to 10,000 cm 2 /g.
15. The method according to claim 14 , wherein the heating rates are from 10 to 6000° C./minute.
16. The method according to claim 14 , wherein the residence time in the tempering step is from 0.01 to 600 minute.
17. The method according to claim 14 , wherein an additional holding time of 1 to 120 minutes, during at 400 to 400° C., is performed during the tempering.
18. The method according to claim 14 , wherein the starting material is selected from the group consisting of high calcium fly ash (calcium content of Class C fly ash), low calcium fly ash (calcium content of Class F fly ash), incineration ash from combustion of municipal wastes both solid and liquid, bottom ash, slag, quartz, sand, gravel, used concrete, asbestos, and mixtures thereof.
19. The method according to claim 14 , wherein the autoclaved product is tempered at a temperature from 400 to 550° C.
20. The method according to claim 11 , wherein the autoclaved product is tempered at a temperature from 400 to 495° C.
21. The method according to claim 11 , wherein a heating rates are from 20 to 100° C./minute.
22. The method according to claim 11 , wherein a residence time in the tempering step is from 1 to 120 minutes.
23. The method according to claim 11 , wherein the residence time in the tempering step is from 5 to 60 minutes.
24. The method according to claim 11 , wherein an additional holding time of 10 to 60 minutes, during heating at 400 to 440° C., is performed during tempering.
25. The method according to claim 11 , wherein the starting material has a molar ratio Ca/(Si+Al+Fe) ranging from 1.5 to 2.5 of about 2.
26. The method according to claim 11 , wherein hydrothermal treatment in the autoclave is carried out at a temperature ranging from 150 to 250 ° C.
27. The method according to claim 14 , further comprising mechanically treating the starting material to optimize particle size and particle size distribution.
28. The method according to claim 14 , wherein further elements or oxides, sodium, potassium, boron, sulphur, phosphorous, or a combination thereof, are added in an amount of 0.1 to 30% by weight while mixing the starting materials or in a subsequent step.
29. The method according to claim 14 , wherein the starting material mixture is seeded with seed crystals which contain calcium silicate hydrate, Portland clinker, granulated blast furnace slag, magnesium silicates, calcium sulphate aluminate (belite) cement, sodium silicate, glass powder, or mixtures thereof.
30. The method according to claim 14 , wherein the starting material has a molar ratio Ca/(Si+Al+Fe) from 1.5 to 2.5.
31. The method according to claim 11 , wherein hydrothermal treatment in the autoclave is carried out for 16 to 32 hours.