Method for producing ternesite
The present invention relates to the production of ternesite clinkers containing 20 to 95% by weight C 5 S 2 $ and less than 15% by weight C 4 A 3 $, and to the use of ternesite as an additive to hydraulic and/or latent hydraulic and/or pozzolanic materials.
1. A method for producing a ternesite clinker, comprising sintering a raw meal mixture, which contains at least sources for CaO, SiO 2 , and SO 3 , wherein a temperature during sintering is adjusted in the range of 900 to 1300° C. such that the ternesite clinker has a content of C 5 S 2 $ ranging from 20 to 95% by weight and a content of C 4 (A x F (1-x) ) 3 $, with x being 0.1 to 1, of less than 15% by weight, in each case relative to the total weight of the clinker.
2. The method according to claim 1 , wherein the raw meal mixture additionally contains sources for Al 2 O 3 and Fe 2 O 3 .
3. The method according to claim 1 , further comprising stabilizing the C 5 S 2 $ by adding one or more foreign ions selected from the group consisting of halogens, nonmetals, alkali and alkaline earth metals, substances from the transition metals and metalloids, and metals to crystal structure of C 5 S 2 $.
4. The method according to claim 1 , further comprising adding a material that supplies mineralizers to the raw meal.
5. The method according to claim 1 , further comprising setting a heating rate in the range of 10 to 6000° C./minute.
6. The method according to claim 3 , wherein the temperature during sintering ranges between 1100 and 1300° C.
7. The method according to claim 1 , wherein the temperature during sintering ranges from 900 to 1200° C.
8. The method according to claim 1 , wherein, in addition to C 5 S 2 $ and C 4 (A x F (1-x) ) 3 $, the clinker contains 0 to 30% by weight C 2 (A y F (1-y) ), with y ranging from 0.2 to 0.8, 0 to 20% by weight reactive aluminates, 0 to 25% by weight periclase (M), and 0 to 30% by weight secondary phases, relative to the total amount of clinker.
9. The method according to claim 8 , wherein at least one X-ray amorphous phase or a glassy phase is present as a secondary phase in the range of 1 to 10% by weight.
10. The method according to claim 1 , wherein the ternesite clinker is ground to a degree of fineness (according to Blaine) ranging from 2000 cm 2 /g to 6000 cm 2 /g.
11. The method according to claim 1 , wherein the ternesite clinker is ground to a degree of fineness (according to Blaine) ranging from 5000 to 10000 cm 2 /g.
12. The method according to claim 1 , wherein the ternesite clinker is ground to a degree of fineness (according to Blaine) of more than 10000 cm 2 /g, and 3 to 99% of a phase content of the clinker is present as an X-ray amorphous phase.
13. The method according to claim 4 , wherein the material is selected from the group consisting of phosphate, fluoride, alkali, nitrate, chloride, and mixtures thereof.
14. The method according to claim 1 , wherein the temperature during sintering ranges from 1050 to 1150° C.
15. The method according to claim 9 , wherein the X-ray amorphous phase or glassy phase is present in the range from 2 to 8% by weight.
16. The method according to claim 15 , wherein the X-ray amorphous phase or glassy phase is present in the range from 3 to 5% by weight.
17. The method according to claim 10 , wherein the degree of fineness ranges from 3000 cm 2 /g to 5000 cm 2 /g.
18. The method according to claim 11 , wherein the degree of fineness ranges from 7000 cm 2 /g to 9000 cm 2 /g.
19. The method according to according to claim 12 , wherein 5 to 50% of the phase content of the clinker is present as an X-ray amorphous phase.
20. The method according to claim 3 , wherein the temperature during sintering ranges from 1050 to 1150° C.
21. The method according to according to claim 9 , wherein the ternesite clinker is ground to a degree of fineness (according to Blaine) ranging from 5000 to 10000 cm 2 /g.