Carbonized brick of recycled concrete powders and preparation method thereof
US-2023364824-A1 · Nov 16, 2023 · US
US12415756B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12415756-B2 |
| Application number | US-202217994198-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 25, 2022 |
| Priority date | Dec 16, 2021 |
| Publication date | Sep 16, 2025 |
| Grant date | Sep 16, 2025 |
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A method of manufacturing inorganic binder by reduction furnace slag includes a raw material preparation step, a stirring step, a maintaining step and a drying step. The raw material preparation step is to provide a powder mixture containing 30 wt % to 55 wt % of reduction furnace slag, and 45 wt % to 70 wt % of glass powder. The stirring step is to place the powder mixture in a mixing tank, and add an alkali activator to the mixing tank to stir and react to form mixed slurry. The alkali equivalent (AE) of the mixed slurry is 2% to 7%, and the water-binder ratio is 0.25 to 0.4. The maintaining step is to place the mixed slurry in a high-temperature and high pressure maintaining environment for a maintaining time to get a binder. The drying step is to dry the binder.
Opening claim text (preview).
What is claimed is: 1. A method of manufacturing an inorganic binder by reduction furnace slag, comprising: a raw material preparation step: providing a powder mixture containing 30 wt % to 55 wt % of reduction furnace slag powder and 45 wt % to 70 wt % of glass powder, wherein the glass powder contains more than 85 wt % of SiO 2 , and the reduction furnace slag powder contains 26 wt % to 62 wt % of CaO, 20 wt % to 32 wt % of SiO 2 and 1.8 wt % to 12.5 wt % of Al 2 O 3 ; a stirring step: placing the powder mixture in a mixing tank, and adding an alkali activator to the mixing tank to stir and react to form a mixed slurry, wherein an alkali equivalent (AE) of the mixed slurry is 2% to 7%, and a water-binder ratio is 0.25 to 0.4; a maintaining step: placing the mixed slurry in a high-temperature and high-pressure maintaining environment for a maintaining time to get a binder, wherein the high-temperature and high-pressure maintaining environment is a temperature of 80 to 250° C. and a pressure of 0.3 to 2.5 MPa, and the maintaining time is 0.5 to 24 hours; and a drying step: drying the binder to remove excess water, to thereby obtain an inorganic binder cured solid; wherein the alkali equivalent is defined as Equation (1), and the water-binder ratio is defined as Equation (2), alkali equivalent = Weight of Na 2 O in alkali activator Weight of powder mixture ⋆ 100 % ; and Equation ( 1 ) water - binder ratio ( W / B ) = Weight of water in alkali activator + weight of additional water Weight of solid in alkali activator + weight of powder mixture . Equation ( 2 ) 2. The method of manufacturing an inorganic binder by reduction furnace slag according to claim 1 , wherein the alkali activator is NaOH, and the alkali equivalent of the mixed slurry is 4% to 6%. 3. The method of manufacturing an inorganic binder by reduction f
Silicates, e.g. glass · CPC title
Heat treatment, e.g. precalcining, burning, melting; Cooling {(aspects only relating to the installation F27B)} · CPC title
Dehydrating; Forming, e.g. granulating (apparatus for granulating B01J2/00) · CPC title
Metallurgical slag · CPC title
Production of cement, e.g. improving or optimising the production methods; Cement grinding · CPC title
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