Clinker substitute based on calcined clay

• US 8,906,155 B2
• Filed: 02/24/2012
• Issued: 12/09/2014
• Est. Priority Date: 03/18/2011
• Status: Expired due to Fees

• Current Assignee: Outotec Oyj (Metso Outotec Oyj)
• Original Assignee: Outotec Oyj (Metso Outotec Oyj)
• Inventors: Gasafi, Edgar, Missalla, Michael
• Primary Examiner(s): Green, Anthony J
• Application Number:
  US14/005,280
• Publication Number:
  US 20140000491A1
• Time in Patent Office: 1,019 Days
• Field of Search: 106/486, 106/811, 106/457, 501/141, 501/150
• US Class Current: 106/811
• CPC Class Codes: C04B 14/10 Clay sepiolite C04B14/042; grog C04B18/025
• CPC Class Codes: C04B 20/04 Heat treatment
• CPC Class Codes: C04B 2111/00017 Aspects relating to the protection of the environment
• CPC Class Codes: C04B 28/04 Portland cements
• CPC Class Codes: C04B 7/13 Mixtures thereof with inorganic cementitious materials, e.g. Portland cements
• CPC Class Codes: C04B 7/40 Dehydrating; Forming, e.g. granulating apparatus for granulating B01J2/00
• CPC Class Codes: C04B 7/522 After-treatment of ground cement C04B7/368 takes precedence
• CPC Class Codes: Y02P 40/10 Production of cement, e.g. improving or optimising the production methods; Cement grinding

Abstract

A method for producing a clinker substitute for use in cement production includes predrying clay with an iron content >1.5 wt-% in a form of iron oxides and a kaolinite content <40 wt-% to a moisture <10 wt-%. The clay is comminuted to a grain size <2 mm. The clay is calcined by thermal treatment in a furnace at a temperature of 600 to 1000° C. The clay is thermally treated under reducing conditions at a temperature of 600 to 1000° C. so as to form a reduction product. The reduction product is intermediately cooled to a temperature <300° C. and finally cooled.

Claims

1. A method for producing a clinker substitute for use in cement production, the method comprising:

a) predrying clay with an iron content >

1.5 wt-% in a form of iron oxides and a kaolinite content <

40 wt-% to a moisture <

10 wt-%;

b) comminuting the clay to a grain size <

2 mm;

c) calcining the clay by thermal treatment in a furnace at a temperature of 600 to 1000°

C.;

d) thermally treating the clay under reducing conditions at a temperature of 600 to 1000°

C. so as to form a reduction product;

e) intermediately cooling the reduction product to a temperature <

300°

C.; and

f) finally cooling the reduction product.

2. The method according to claim 1, wherein the clay in step a) has a CaO content >

0.1 wt-%.

3. The method according to claim 1, wherein the intermediate cooling of the reduction product in step e) is effected under oxygen exclusion.

4. The method according to claim 1, wherein, during the intermediate cooling of the reduction product in step e), oil is introduced as an additional reducing agent.

5. The method according to claim 1, wherein the calcination in step c) is effected in a fluidized-bed reactor, a rotary kiln, a suspension calciner or a multiple-hearth roaster.

6. The method according to claim 1, wherein in an external combustion chamber a fuel is burnt and a combustion product produced is used for carrying out the thermal treatment in at least one of steps c) and d).

7. The method according to claim 6, wherein the combustion is carried out in a plurality of stages including at least one first stage in which the combustion is effected under reducing conditions and at least one second stage in which the combustion is effected under oxidizing conditions.

8. The method according to claim 7, wherein a combustion product produced in the at least one first stage is used as reduction gas during the thermal treatment in step d).

9. The method according to claim 7, wherein a combustion product produced in the at least one second stage is used as hot gas during the calcination in step c).

10. The method according to claim 1, wherein the clay is preheated in one or more preheating stages prior to the calcination.

11. A clinker substitute containing calcined clay, wherein the calcined clay is derived from calcination of a clay that contains <

40 wt-% kaolinite and >

1.5 wt-% iron in a form of iron oxides, and wherein >

90 wt-% of the iron oxides contained in the clay are present as magnetite (Fe₃O₄).

12. The clinker substitute according to claim 11, wherein the clay contains no hematite (Fe₂O₃).

13. The clinker substitute according to claim 11, wherein the clay contains >

0.1 wt-% CaO.

14. The clinker substitute according to claim 11, wherein no limestone or no kaolin is added to the clay.

15. The clinker substitute according to claim 11, wherein the clinker substitute is present in cement, mortar or concrete.

16. Cement containing the clinker substitute according to claim 11.

17. Mortar or concrete containing the cement according to claim 16.

18. A method for producing a cement clinker or a construction material containing the cement clinker, wherein the construction material is cement, mortar or concrete, comprising the step of replacing 10 to 40 wt-% of a conventional cement clinker by the clinker substitute according to claim 11.

19. A structure containing the mortar or cement according to claim 16.