IP Library Patent Application 18874463
Patent Application
App. No. 18/874,463

METHOD OF AT LEAST PARTLY CALCINING A RAW MATERIAL IN A PROCESS OF PRODUCING A CEMENTITIOUS MATERIAL

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Patent No.
US None
App. No.
18/874,463
Abstract

A method of at least partly calcining a raw material in a process of producing a cementitious material, includes providing a first calcination device that is heated by a plasma torch ejecting a plasma jet, introducing a flow of raw material into the first calcination device, at least partially calcining the raw material in the first calcination device, wherein a first flow of a CO 2 rich gas containing at least 60 vol.-% CO 2 is fed to the plasma torch as a carrier gas for generating the plasma jet, and wherein a second flow of a CO 2 rich gas containing at least 60 vol.-% CO 2 is mixed with the plasma jet in order to adjust the temperature and/or the shape of the plasma jet.

Claims (25)

1 . A method of at least partly calcining a raw material in a process of producing a cementitious material, comprising:

providing a first calcination device that is heated by means of a plasma torch ejecting a plasma jet,

introducing a flow of raw material into the first calcination device,

at least partially calcining the raw material in the first calcination device,

wherein a first flow of a CO 2 rich gas containing at least 60 vol.-% CO 2 is fed to the plasma torch as a carrier gas for generating the plasma jet, and

wherein a second flow of a CO 2 rich gas containing at least 60 vol.-% CO 2 is mixed with the plasma jet in order to adjust the temperature and/or the shape of the plasma jet.

2 . The method according to claim 1 , wherein the flow of raw material is fed into the plasma jet in order to provide a direct heating of the raw material.

3 . The method according to claim 1 , wherein the flow of raw material is introduced into the calcination device by being entrained by the plasma jet.

4 . The method according to claim 1 , wherein the CO 2 rich gas of the first flow and/or of the second flow of CO 2 rich gas additionally contains H2O.

5 . The method according to claim 1 , wherein at least partly calcining the raw material comprises decarbonating a raw material that contains a metal carbonate, thereby releasing CO 2 rich exhaust gas, wherein said CO 2 rich exhaust gas is drawn off from the first calcination device and at least partly used for said first and/or second flow of the CO 2 rich gas.

6 . The method according to claim 1 , wherein the CO 2 rich gas of the first flow and/or of the second flow of CO 2 rich gas contains at least 80 vol.-% CO 2 .

7 . The method according to claim 1 , wherein a ratio of the a sum of the first flow and the second flow of the CO 2 rich gas to the electric power used to operate the plasma torch is adjusted to 0.25-5.0, expressed as kWh/Nm 3 .

8 . The method according to claim 1 , further comprising introducing the partly calcined raw material into a second calcination device and further calcining the material in order to obtain a cementitious material.

9 . The method according to claim 8 , wherein the first calcination device is a precalciner of a cement manufacturing plant and the second calcination device is rotary kiln of the cement manufacturing plant.

10 . The method according to claim 1 , wherein the flow of raw material is preheated before being introduced into the first calcination device.

11 . The method according to claim 10 , wherein a CO 2 rich exhaust gas is withdrawn from the first calcination device, and said CO 2 rich exhaust gas is used as said heat exchanging fluid to preheat the raw material.

12 . The method according to claim 5 , wherein the CO 2 rich exhaust gas is re-heated in a heat storage and/or generating device and introduced into the first calcination device.

13 . The method according to claim 12 , wherein the heat storage device is loaded with thermal energy by means of a heating device that is operated by electrical energy.

14 . The method according to claim 8 , wherein the cementitious material is introduced into a cooling device, in which the CO 2 rich exhaust gas is used to cool the cementitious material, while the CO 2 rich exhaust gas is re-heated and then introduced into the second calcination device.

15 . The method according to claim 8 , wherein the second calcination device is heated by electrical energy and/or by combusting a renewable fuel and/or by combusting hydrogen.

16 . The method according to claim 1 , wherein the raw material consists of or comprises natural cement raw meal components, clay, or waste materials.

17 . The method according to claim 5 , wherein the metal carbonate is CaCO 3 .

18 . The method according to claim 7 , wherein the ratio of the sum of the first flow and the second flow of the CO 2 rich gas to the electric power used to operate the plasma torch is from 1.0 to 3.0 expressed as kWh/Nm 3 .

19 . The method according to claim 8 , wherein the cementitious material is a cement clinker.

20 . The method according to claim 10 , wherein the preheating is carried out by bringing a heat exchanging fluid into a heat exchanging relationship with the raw material, while the heat exchanging fluid is cooled.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 14, 2025
From: HOLCIM TECHNOLOGY LTD
To: AMRIZE TECHNOLOGY SWITZERLAND LLC
Reel/Frame 073207/0820 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 12, 2024
From: SEYLER, LAURENT; BOES, KARL-HEINZ; STOFFEL, BEAT
To: HOLCIM TECHNOLOGY LTD
Reel/Frame 069570/0720 →