Method and device for carbonation
A method for converting a starting material containing at least 40 wt.-% of calcium silicon (hydr)oxide phases and calcium aluminum (hydr)oxide phases into an SiO2 rich SCM and a calcium carbonate additive includes the steps: providing the starting material with a D 90 of ≤1 mm, mixing the starting material with water or adjusting the water content to provide a starting material slurry having a solid:liquid weight ratio from 2:1 to 1:100, passing the starting material slurry together with carbon dioxide into a gravity separation reactor, subjecting the starting material slurry and carbon dioxide to centrifugal motion inside the reactor, and removing a heavy slurry from a first outlet of the reactor, removing a light slurry of lower density particles from a second outlet of the reactor, and removing liquid at a third outlet of the reactor.
1 . A method for converting a starting material containing waste materials and/or by-products, selected from the group consisting of concrete demolition waste, material left over from concreting, slag, ash, muds, and mixtures thereof, wherein the starting material contains at least 40 wt.-% of calcium silicon (hydr)oxide phases and calcium aluminum (hydr)oxide phases, said phases being selected from the group consisting of calcium silicon hydrates, alite, belite, rankinite, wollastonite, hydrogarnet, ettringite, calcium aluminum hydrates, calcium silicon/aluminum (hydr)oxides with additional elements, and mixtures thereof, into an SiO 2 rich supplementary cementitious material and a calcium carbonate additive comprising the steps of:
providing the starting material with a D 90 of ≤1 mm;
mixing the starting material with water or adjusting a water content of the starting material to provide a starting material slurry having a solid: liquid ratio from 2:1 to 1:100;
passing the starting material slurry into a gravity separation reactor together with carbon dioxide;
subjecting the starting material slurry and carbon dioxide to centrifugal motion provided by adjusting a rotational speed to range from 10,000 to 150,000 rev min-inside the reactor; and
removing a heavy slurry of higher density particles comprising the calcium carbonate additive formed by reaction of carbon dioxide with calcium ions dissolved or leached from the starting material from a first outlet of the reactor, removing a light slurry of lower density particles comprising the undissolved SiO 2 rich remains of the starting material from a second outlet of the reactor, and removing liquid from a third outlet of the reactor.
2 . The method according to claim 1 , wherein the starting material has a D 90 of ≤500 μm.
3 . The method according to claim 1 , wherein the starting material comprises at least 50 wt.-% of calcium silicon (hydr)oxide phases and calcium aluminum (hydr)oxide phases.
4 . The method according to claim 1 , wherein the carbon dioxide is at least partly introduced in gaseous form with a concentration from 1 to 100 Vol.-%.
5 . The method according to claim 1 , wherein the carbon dioxide is at least partly introduced in the form of a solution with a concentration from 0.1 to 20 wt.-%.
6 . The method according to claim 1 , wherein the carbon dioxide gas is an exhaust gas.
7 . The method according to claim 1 , wherein the liquid removed from the third outlet of the reactor is used to at least partly replace water for mixing with the starting material to form the starting material slurry.
8 . The method according to claim 2 , wherein the starting material slurry has a D 90 of ≤250 μm.
9 . The method according to claim 2 , wherein the starting material slurry has a D 90 of ≤125 μm.
10 . The method according to claim 1 , wherein the starting material is obtained from concrete demolition waste and/or material left over from concreting.
11 . The method according to claim 3 , wherein the starting material comprises at least 60 wt.-%, of calcium silicon (hydr)oxide phases and calcium aluminum (hydr)oxide phases.
12 . The method according to claim 1 , wherein the starting material comprises at least 70 wt.-% of calcium silicon (hydr)oxide phases and calcium aluminum (hydr)oxide phases.
13 . The method according to claim 4 , wherein the carbon dioxide concentration ranges from 5 to 90 Vol.-%.
14 . The method according to claim 5 , wherein the carbon dioxide concentration ranges from 0.5 to 10 wt.-%.
15 . The method according to claim 6 , wherein the exhaust gas is from cement manufacturing and/or from a gas fired power plant and/or a coal fired power plant.
16 . The method according to claim 8 , wherein the starting material is obtained from concrete demolition waste and/or material left over from concreting and comprises at least 60 wt.-%, of calcium silicon (hydr)oxide phases and calcium aluminum (hydr)oxide phases.