System and method for producing cement clinker
US-2021372700-A1 · Dec 2, 2021 · US
US2023131508A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023131508-A1 |
| Application number | US-202117791877-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 5, 2021 |
| Priority date | Jan 9, 2020 |
| Publication date | Apr 27, 2023 |
| Grant date | — |
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An apparatus for thermally treating mineral solids includes a preheater, a separating apparatus arranged at an outlet of an entrained flow reactor, and a thermal treatment zone at an outlet of a gas stream of the separating apparatus, with an outlet of the treatment zone being connected to an inlet of the preheater for the gas stream. A process may involve preheating a mineral material, thermally treating the mineral material in an entrained flow reactor in a reducing atmosphere for reducing coloring metal compounds, separating a solid/gas mixture from the entrained flow reactor in a separating apparatus, oxidizing reducing constituents of a gas from the separating apparatus in a thermal treatment zone between the separating apparatus and the preheater via supplied oxygen, and supplying gas emerging from the thermal treatment zone to the preheater and thereby utilizing thermal energy recovered in the thermal treatment zone by transfer to mineral material
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1 .- 12 . (canceled) 13 . An apparatus that is configured to thermally treat mineral solids, the apparatus comprising: a preheater; an entrained flow reactor comprising a reducing agent supply line; a separating apparatus disposed at an outlet of the entrained flow reactor; and a thermal treatment zone disposed at an outlet of a gas stream of the separating apparatus, wherein the thermal treatment zone comprises a second supply apparatus for oxygen, wherein the thermal treatment zone is configured for reacting a reducing agent supplied by the reducing agent supply line with the oxygen, wherein an outlet of the thermal treatment zone is connected to an inlet of the preheater for a gas stream. 14 . The apparatus of claim 13 wherein the reducing agent supply line is a supply apparatus for the reducing agent. 15 . The apparatus of claim 13 wherein the reducing agent supply line is a combustion apparatus that supplies more fuel than there is oxygen present, the combustion apparatus being configured to generate reducing constituents. 16 . The apparatus of claim 13 comprising a transfer apparatus for the mineral solids, which are heated in the preheater, for transfer from the preheater to the entrained flow reactor. 17 . The apparatus of claim 13 wherein the thermal treatment zone is cylindrical. 18 . The apparatus of claim 13 wherein the thermal treatment zone is tubular and extends vertically above the separating apparatus. 19 . The apparatus of claim 13 wherein the thermal treatment zone includes a first supply apparatus for a fuel. 20 . The apparatus of claim 13 wherein the preheater is a cyclone preheater. 21 . The apparatus of claim 13 wherein the preheater is a two-stage cyclone preheater. 22 . A process for thermally treating mineral material that comprises iron compounds and/or chromium compounds, the process comprising: preheating a mineral material in a preheater; transferring the mineral material that is heated in the preheater to an entrained flow reactor; thermally treating the mineral material in the entrained flow reactor in a reducing atmosphere for reducing coloring metal compounds during the thermal treatment; separating a solid/gas mixture coming from the entrained flow reactor in a separating apparatus; oxidizing reducing constituents of a gas coming from the separating apparatus in a thermal treatment zone between an outlet of a gas stream of the separating apparatus and an inlet of the preheater for the gas stream by way of supplied oxygen; and supplying the gas emerging from the thermal treatment zone to the preheater and thereby utilizing thermal energy recovered in the thermal treatment zone by transfer to the mineral material. 23 . The process of claim 22 wherein the oxidizing occurs at a temperature of 700° C. to 1000° C. and over a period of 1 s to 10 s. 24 . The process of claim 22 comprising supplying a fuel to the gas in the oxidizing step. 25 . The process of claim 22 comprising guiding a flow of the mineral material around the thermal treatment zone.
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