Method of producing a synthetic carbonated mineral component in a cement manufacturing plant

Patent metadata

Field	Value
Publication number	US-2024092691-A1
Application number	US-202118256829-A
Country	US
Kind code	A1
Filing date	Dec 9, 2021
Priority date	Dec 10, 2020
Publication date	Mar 21, 2024
Grant date	—

Abstract

A method of producing a synthetic carbonated mineral component in a cement manufacturing plant, includes providing a carbonatable substance from an external source, introducing the carbonatable substance into an exhaust gas installation of the cement manufacturing plant for contacting the carbonatable substance with CO 2 enriched exhaust gas, carbonating the carbonatable substance by reacting the carbonatable substance with CO 2 contained in the CO 2 enriched exhaust gas, thereby obtaining the synthetic carbonated mineral component, and removing the synthetic carbonated mineral component from the exhaust gas installation.

First claim

1 . A method of producing a synthetic carbonated mineral component in a cement manufacturing plant, wherein the cement manufacturing plant comprises a calcination device for producing Portland clinker by decarbonating cement raw meal while releasing a CO 2 enriched exhaust gas and further comprising an exhaust gas installation for directing a flow of the CO 2 enriched exhaust gas from the calcination device to an exhaust stack of the cement manufacturing plant,
wherein the method comprises:
a) providing a carbonatable substance from an external source,
b) introducing the carbonatable substance into the exhaust gas installation for contacting the carbonatable substance with the CO 2 enriched exhaust gas,
c) carbonating the carbonatable substance by reacting the carbonatable substance with CO 2 contained in the CO 2 enriched exhaust gas, thereby obtaining the synthetic carbonated mineral component, and
d) removing the synthetic carbonated mineral component from the exhaust gas installation.

2 . The method according to claim 1 , wherein the exhaust gas installation comprises a cement kiln bypass installation for extracting kiln bypass dust and exhaust gas from the calcination device, and a bypass filter connected to an exhaust end of the cement kiln bypass installation, wherein the introducing of the carbonatable substance into the exhaust gas installation comprises introducing the carbonatable substance into the cement kiln bypass installation upstream of the bypass filter, and wherein the removing of the synthetic carbonated mineral component from the exhaust gas installation comprises separating the synthetic carbonated mineral component from the exhaust gas by means of said bypass filter and removing the synthetic carbonated mineral component from the bypass filter.

3 . The method according to claim 2 , wherein the cement kiln bypass installation comprises a quenching chamber for cooling the kiln bypass dust and the exhaust gas, and wherein the carbonatable substance is introduced into the quenching chamber.

4 . The method according to claim 3 , wherein a quenching air duct is connected to the quenching chamber for introducing quenching air into the quenching chamber, and wherein the carbonatable substance is introduced into the quenching chamber via the quenching air duct.

5 . The method according to claim 1 , wherein the cement manufacturing plant comprises a preheater for preheating the cement raw meal in counter or cross current to the exhaust gas and optionally an exhaust gas conditioning tower for conditioning the exhaust gas coming from the preheater, and wherein the exhaust gas installation comprises an exhaust gas duct arranged downstream of the preheater or the exhaust gas conditioning tower for directing the exhaust gas to a main filter, and wherein the introducing of the carbonatable substance into the exhaust gas installation comprises introducing the carbonatable substance into the exhaust gas flow at a location between the preheater and the main filter, and wherein the removing of the synthetic carbonated mineral component from the exhaust gas installation comprises separating the synthetic carbonated mineral component from the exhaust gas by means of said main filter and removing the synthetic carbonated mineral component from the main filter.

6 . The method according to claim 5 , wherein the carbonatable substance is introduced into the exhaust gas conditioning tower.

7 . The method according to claim 5 , wherein the carbonatable substance is introduced into a mill fed by preheater exhaust gas, for drying, grinding and/or carbonating the carbonatable substance.

8 . The method according to claim 5 , wherein the carbonatable substance is introduced into the exhaust gas duct upstream of the main filter.

9 . The method according to claim 1 wherein the synthetic carbonated mineral component, after step d) is re-introduced into the exhaust gas installation and steps c) and d) are repeated.

10 . The method according to claim 1 , wherein carbonation is conducted until a CaCO 3 content of the carbonatable substance has increased by at least 5 wt. %.

11 . The method according to claim 1 , wherein the synthetic carbonated mineral component is mixed with the Portland clinker coming from the calcination device.

12 . The method according to claim 11 , wherein the synthetic carbonated mineral component and the Portland clinker are co-ground in a cement mill of the cement manufacturing plant.

13 . The method according to claim 1 , wherein the carbonatable substance is a mineral component having a total metal oxide content of at least 10 wt. %.

14 . The method according to claim 1 , wherein the carbonatable substance is a concrete mud that is obtained by recuperating mud from a decantation basin in a concrete ready-mix plant and reducing a water content of the mud.

15 . The method according to claim 1 , wherein the carbonatable substance is obtained from recycled concrete by crushing recycled concrete, separating a fine fraction of said crushed recycled concrete from a coarse fraction and using the fine fraction as said carbonatable material, wherein the fine fraction is composed of particles having a particle size of 0-4 mm.

16 . The method according to claim 10 , wherein carbonation is conducted until the CaCO 3 content of the carbonatable substance has increased by at least 10 wt.-%.

17 . The method according to claim 13 , wherein the carbonatable substance is a mineral component having a total metal oxide content of at least 30 wt.-%.

18 . The method according to claim 15 , wherein the fine fraction is composed of particles having a particle size of 0-3 mm.

19 . The method according to claim 18 , wherein fine fraction is composed of particles having a particle size of 0-2 mm.

Assignees

• Holcim Technology Ltd

Inventors

• Durand Thomas
• Morin Vincent
• Huet Bruno
• Meyer Vincent

Classifications

• C04B7/367 Primary

  Avoiding or minimising carbon dioxide emissions · CPC title

• C04B7/02

  Portland cement · CPC title

• C04B7/246

  from waste building materials, e.g. waste asbestos-cement products, demolition waste · CPC title

• C04B7/432

  Preheating without addition of fuel · CPC title

• C04B7/52

  Grinding {; After-treatment of ground cement} · CPC title