Method of producing cement clinker and a second calcined material

Patent metadata

Field	Value
Publication number	US-2023002277-A1
Application number	US-202017781634-A
Country	US
Kind code	A1
Filing date	Dec 18, 2020
Priority date	Dec 18, 2019
Publication date	Jan 5, 2023
Grant date	—

Abstract

A method of producing cement clinker and a second calcined material, wherein the cement clinker is produced in a first production line and the second calcined material is produced from a raw material in a second production line by carrying out the following procedures e) optionally drying the raw material in a dryer, g) calcining the optionally dried raw material in a rotary kiln to obtain the second calcined material, wherein the sensible heat of a hot gas in the first production line is used as a heat source in the calcining step g) for calcining the raw material, and wherein the rotary kiln exhaust gas coming from the calcining step g) is introduced into the first production line for the secondary combustion of the rotary kiln exhaust gas.

First claim

1 . A method of producing a first calcined material, which is cement clinker, and a second calcined material, wherein the cement clinker is produced in a first production line by carrying out the following steps:
a) preheating raw meal in a preheater in counter current flow to hot exhaust gases coming from a clinker furnace, b) optionally pre-calcining the preheated raw meal in a pre-calciner, c) calcining the preheated and optionally pre-calcined raw meal in the clinker furnace in counter current flow to combustion gases of a clinker furnace burner to obtain cement clinker, d) cooling the cement clinker in a clinker cooler,
wherein the second calcined material is produced from a raw material in a second production line by carrying out the following steps:
e) optionally drying a raw material in a dryer,
f) optionally crushing the optionally dried raw material in a crusher,
g) calcining the optionally dried and optionally crushed raw material in a rotary kiln to obtain the second calcined material,
h) optionally cooling the second calcined material in a cooler,

wherein a sensible heat of a hot gas in the first production line is used as a heat source in the calcining step g) for calcining the raw material, and
wherein the rotary kiln exhaust gas coming from the calcining step g) is introduced into the first production line for the secondary combustion of the rotary kiln exhaust gas.

2 . The method according to claim 1 , wherein a clinker cooler off-gas from the clinker cooler is used as said heat source in the calcining step g).

3 . The method according to claim 1 , wherein the rotary kiln exhaust gas is introduced into the pre-calciner or the preheater of the first production line.

4 . The method according to claim 1 , wherein the raw material is selected from sludges resulting from washing of sand or aggregates, asphalt, (waste) gypsum, contaminated earth, wet fly ash, other waste or demolition materials, road cleaning sludges, filter cakes from treatment processes of soil and waste washing, and combinations thereof.

5 . The method according to claim 1 , wherein the raw material is dried in said drying step e) for reducing the amount of free water to <20 wt-%.

6 . The method according to claim 1 , wherein the sensible heat of a hot gas in the first production line is used as a heat source in the drying step e) for drying the raw material.

7 . The method according to claim 1 , wherein the dryer and the cooler of the second production line are operated in a heat exchanging relationship so that the sensible heat drawn from the second calcined material during the cooling step h) is used as a heat source for drying the raw material in the drying step e).

8 . The method according to claim 1 , wherein the dryer and the cooler of the second production line are operated in a heat exchanging relationship so that the a loss of sensible heat to the raw material during the drying step e) is used as a cooling source for cooling the second calcined material in the cooling step h).

9 . The method according to claim 1 , wherein a drying screw is used for drying the raw material in the drying step e).

10 . The method according to claim 1 , wherein fuel is burnt in a burner of the rotary kiln for calcining the raw material in step g).

11 . A system comprising a first production line for producing a first calcined material, which is clinker, and a second production line for producing a second calcined material, wherein the first production line comprises:
a) a preheater for preheating raw meal in counter current flow to hot exhaust gases coming from a clinker furnace, b) optionally a pre-calciner for pre-calcining the preheated raw meal, c) a clinker furnace for calcining the preheated and optionally pre-calcined raw meal in counter current flow to combustion gases of a clinker furnace burner to obtain cement clinker, d) a clinker cooler for cooling the cement clinker, wherein the second production line comprises: e) optionally a dryer for drying a raw material, f) optionally a crusher for crushing the optionally dried raw material, g) a rotary kiln for calcining the optionally dried and optionally crushed raw material to obtain the second calcined material, h) optionally a cooler for cooling the second calcined material,
wherein the first production line and the second production line are connected by a first heat exchanging pipe for feeding a sensible heat of a hot gas from the first production line to the rotary kiln as a heat source for calcining the raw material, and
wherein the first production line and the second production line are connected by a second pipe for introducing a rotary kiln exhaust gas coming from the rotary kiln into the first production line for the secondary combustion of the rotary kiln exhaust gas.

12 . The system according to claim 11 , wherein the first heat exchanging pipe is in fluid communication with a clinker cooler of the first production line to feed a clinker cooler off-gas from the clinker cooler as said heat source into the rotary kiln of the second production line.

13 . The system according to claim 11 , wherein the second pipe is in fluid communication with the pre-calciner or the preheater of the first production line for introducing the rotary kiln exhaust gas into the pre-calciner or the preheater, respectively.

14 . The system according to claim 11 , wherein the first production line and the second production line are connected by a third heat exchanging pipe for feeding the sensible heat of a hot gas from the first production line to the dryer as a heat source for drying the raw material.

15 . The system according to claim 11 , wherein the dryer and the cooler of the second production line are connected with each other in a heat exchanging manner so that the sensible heat drawn from the second calcined material in the cooler is used as a heat source for drying the raw material in the dryer.

16 . The system according to claim 11 , wherein the dryer and the cooler of the second production line are connected with each other in a heat exchanging manner so that a loss of sensible heat to the raw material in the dryer is used as a cooling source for cooling the second calcined material in the cooler.

17 . The system according to claim 11 , wherein the dryer is designed as a drying screw, comprising a screw conveyor for conveying the raw material and a heat exchanger surface for transferring heat from a heat exchanger fluid to the raw material while being conveyed.

18 . The system according to claim 11 , wherein the rotary kiln comprises a burner.

19 . The system according to claim 11 , wherein the cooler is designed as a cooling screw, comprising a screw conveyor for conveying the second calcined material and a heat exchanger surface for transferring heat from the second calcined material to a heat exchanger fluid.

20 . The method according to claim 1 , wherein the second calcined material is a material having pozzolanic and/or latent hydraulic properties.

Assignees

• Holcim Technology Ltd

Inventors

• Weihrauch Michael
• Bucher Ernst
• Spuler Andreas
• Kruspan Peter
• Blum Rudy

Classifications

• C04B7/28

  from combustion residues, {e.g. ashes or slags from waste incineration}({C04B7/243} , C04B7/26 take precedence) · CPC title

• C04B7/522

  After-treatment of ground cement (C04B7/368 takes precedence) · CPC title

• C04B7/26

  from raw materials containing flue dust {, i.e. fly ash (C04B7/243 takes precedence)} · CPC title

• C04B7/44

  Burning; Melting · CPC title

• C04B2290/20

  Integrated combined plants or devices, e.g. combined foundry and concrete plant · CPC title