Method of producing a supplementary cementitious material

Patent metadata

Field	Value
Publication number	US-2023406774-A1
Application number	US-202118247702-A
Country	US
Kind code	A1
Filing date	Sep 30, 2021
Priority date	Oct 5, 2020
Publication date	Dec 21, 2023
Grant date	—

Abstract

A method of producing a supplementary cementitious material, includes providing at least one waste material selected from quarry sludge, aggregate washing sludge and road cleaning sludge, removing excess water from said waste material so as to provide a dry waste material, and either: mixing the dry waste material with a source of calcium sulphate to obtain a raw material mixture, and calcining the raw material mixture at a temperature of 700-900° C. to obtain the supplementary cementitious material, or: calcining the dry waste material at a temperature of 700-900° C. to obtain a calcined waste material, and mixing the calcined waste material with a calcined source of calcium sulphate to obtain the supplementary cementitious material.

First claim

1 . A method of producing a supplementary cementitious material, comprising:
providing at least one waste material selected from quarry sludge, aggregate washing sludge and road cleaning sludge, removing excess water from said waste material so as to provide a dry waste material, and either:
mixing the dry waste material with a source of calcium sulphate to obtain a raw material mixture,
calcining the raw material mixture at a temperature of 700-900° C. to obtain the supplementary cementitious material,
or:
calcining the dry waste material at a temperature of 700-900° C. to obtain a calcined waste material,
mixing the calcined waste material with a calcined source of calcium sulphate to obtain the supplementary cementitious material.

2 . The method according to claim 1 , wherein the calcination is carried out at a temperature of 770-830° C. of raw material mixture.

3 . The method according to claim 1 , wherein the calcination is carried out in a fluidized bed for a duration comprised between 5 and 25 minutes, or in a rotary kiln for a duration of 20 to 80 minutes.

4 . The method according to claim 1 , wherein the dry waste material is crushed before being calcined.

5 . The method according to claim 4 , wherein the crushed waste material is sieved to obtain a fine fraction and a coarse fraction and wherein only the fine fraction is calcined.

6 . The method according to claim 5 , wherein the fine fraction does not comprise particles having a particle size >125 μm.

7 . The method according to claim 1 , wherein the supplementary cementitious material is ground after the calcination.

8 . The method according to claim 1 , wherein the source of calcium sulphate is obtained from waste gypsum.

9 . The method according to claim 1 , wherein the raw material mixture has the following composition:
25-55 wt. %, carbonates, 10-30 wt. %, sheet silicates, 15-35 wt. %, silicates other than sheet silicates, 10-15 wt. %, calcium sulphate, expressed as weight percentage of CaSO 4 .

10 . The method according to claim 1 , wherein the raw material mixture consists of 80-95 wt.-% dry waste material selected from dried quarry sludge, aggregate washing sludge, road cleaning sludge, and mixtures thereof, and 5-20 wt.-% waste gypsum.

11 . A supplementary cementitious material comprising calcined waste material selected from quarry sludge, aggregate washing sludge and road cleaning sludge, and a calcined source of calcium sulphate.

12 . The supplementary cementitious material according to claim 11 , which has the following composition:
30-60 wt.-% XRD-amorphous and/or poorly crystalline fraction, 5-35 wt.-% silicates other than calcium silicates and other than sheet silicates, 5-15 wt.-% calcium sulphate, expressed as weight percentage of CaSO 4 , 5-10 wt.-% carbonates, 1-10 wt.-% calcium oxides (free lime) and portlandite, 1-10 wt.-% calcium silicates, such as belite and larnite, 1-10 wt.-% a rest.

13 . A hydraulic binder comprising Portland cement and a supplementary cementitious material obtained by a method according to claim 1 .

14 . The hydraulic binder according to claim 13 , wherein the hydraulic binder comprises 5-50 wt. %, of the supplementary cementitious material.

15 . The hydraulic binder according to claim 13 , wherein the hydraulic binder comprises 50-95 wt. %, Portland cement.

16 . The method according to claim 3 , wherein the calcination is carried out in a fluidized bed for a duration comprised between 10 and 20 minutes, or in a rotary kiln for a duration of 30 to 70 minutes.

17 . The method according to claim 8 , wherein the source of calcium sulphate is obtained from plasterboards.

18 . The method according to claim 9 , wherein the raw material mixture has the following composition:
30-40 wt.-% carbonates, 22-28 wt.-% sheet silicates, 25-30 wt.-% silicates other than sheet silicates, 10-11 wt.-% calcium sulphate, expressed as weight percentage of CaSO 4 .

19 . The method according to claim 18 , wherein the sheet silicates are clay minerals, and the silicates other than sheet silicates include feldspar and quartz.

20 . The method according to claim 10 , wherein the raw material mixture consists of 80-95 wt.-% dry waste material selected from dried quarry sludge, aggregate washing sludge, road cleaning sludge, and mixtures thereof, and 10-18 wt.-% waste gypsum.

Assignees

• Holcim Technology Ltd

Inventors

• Kruspan Peter
• Bucher Ernst
• Lunk Peter
• Weihrauch Michael

Classifications

• C04B28/14 Primary

  containing calcium sulfate cements {(gypsum-paper plates E04C)} · CPC title

• C04B14/043

  Alkaline-earth metal silicates, e.g. wollastonite · CPC title

• C04B14/26

  Carbonates · CPC title

• C04B18/04

  Waste materials; Refuse · CPC title

• C04B14/10

  Clay {(sepiolite C04B14/042; grog C04B18/025)} · CPC title