Ground granulated blast furnace slag based binder presenting both ettringite and stratlingite phases at the hardened state
US-2025304498-A1 · Oct 2, 2025 · US
US2024116810A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024116810-A1 |
| Application number | US-202218263033-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 22, 2022 |
| Priority date | Mar 19, 2021 |
| Publication date | Apr 11, 2024 |
| Grant date | — |
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The present application describes a process for the continuous production of alpha-calcium sulphate hemihydrate, the process comprising the steps of: providing particulate gypsum; providing water; mixing the particulate gypsum and the water to form a gypsum slurry; and maintaining said gypsum slurry under raised pressure and temperature to convert the particulate gypsum into alpha-calcium sulphate hemihydrate and provide an alpha-calcium sulphate hemihydrate slurry. Additionally, the particulate gypsum comprises a D10 value greater than or equal to 2 μm, a D90 value smaller than or equal to 90 μm and a D50 value smaller than or equal to 25 μm. Particulate gypsum for use in the process is also provided.
Opening claim text (preview).
1 - 15 . (canceled) 16 . A process for the continuous production of alpha-calcium sulphate hemihydrate, the process comprising: providing particulate gypsum; providing water; mixing said particulate gypsum and said water to form a gypsum slurry; and maintaining said gypsum slurry under raised pressure and temperature to convert said particulate gypsum into alpha-calcium sulphate hemihydrate and provide an alpha-calcium sulphate hemihydrate slurry, wherein said particulate gypsum has a D10 value greater than or equal to 2 μm, a D90 value smaller than or equal to 90 μm and a D50 value smaller than or equal to 25 μm. 17 . The process of claim 16 , wherein said particulate gypsum has a D50 value smaller than or equal to 20 μm. 18 . The process of claim 17 , wherein said particulate gypsum has a D50 value smaller than or equal to 15 μm. 19 . The process of claim 16 , wherein said raised temperature is in the range 110° C. to 170° C. inclusive. 20 . The process of claim 16 , wherein said raised pressure is in the range 0.15 MPa to 0.80 MPa inclusive. 21 . The process of claim 16 , wherein a gypsum particle within said gypsum slurry is maintained under conditions of raised temperature and pressure for a mean residence time within the range 10 minutes to 120 minutes inclusive. 22 . The process of claim 16 , wherein said gypsum slurry comprises a water to gypsum ratio of between 0.4 and 1.5 by weight inclusive. 23 . The process of claim 16 , wherein said gypsum slurry comprises a Brookfield viscosity in the range of 15 to 0.5 cP inclusive at 80° C. 24 . The process of claim 16 , wherein the process further comprises grinding said particulate gypsum to reduce the size of particles therein. 25 . The process of claim 16 , wherein providing particulate gypsum comprises substantially continuously providing particulate gypsum. 26 . The process of claim 16 , wherein the providing of water comprises substantially continuously providing water. 27 . The process of claim 16 , wherein the maintaining said gypsum slurry under raised pressure and temperature to convert said particulate gypsum into alpha-calcium sulphate hemihydrate and provide an alpha-calcium sulphate hemihydrate slurry comprises holding said gypsum slurry within a calcination vessel. 28 . The process of claim 16 , wherein the process comprises removing water from said alpha-calcium sulphate hemihydrate slurry. 29 . The process of claim 28 , wherein the providing water comprises mixing the water removed from the alpha-calcium sulphate hemihydrate slurry with additional water. 30 . Particulate gypsum for use in the process of claim 16 , said particulate gypsum having a D10 value greater than or equal to 2 μm, a D90 value smaller than or equal to 90 μm and a D50 value smaller than or equal to 25 μm.
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