Macroporous oxygen carrier solid with an oxide ceramic matrix, method for the preparation thereof, and use thereof for a chemical-looping oxidation-reduction method

Patent metadata

Field	Value
Publication number	US-11717811-B2
Application number	US-201716471499-A
Country	US
Kind code	B2
Filing date	Dec 21, 2017
Priority date	Dec 23, 2016
Publication date	Aug 8, 2023
Grant date	Aug 8, 2023

Abstract

The invention relates to an oxygen carrier solid, its preparation and its use in a method of combustion of a hydrocarbon feedstock by active mass chemical-looping oxidation-reduction, i.e. chemical-looping combustion (CLC). The solid, which is in the form of particles, comprises an oxidation-reduction active mass composed of metal oxide(s) dispersed in a ceramic matrix comprising at least one oxide with a melting point higher than 1500° C., such as alumina, and has, initially, a specific macroporous texture. The oxygen carrier solid is prepared from an aqueous suspension containing precursor oxide grains for the ceramic matrix that have a specific size, by a spray-drying technique.

First claim

The invention claimed is:

1. An oxygen carrier solid in the form of particles for a process for chemical looping redox combustion of a hydrocarbon feedstock, comprising:
a redox active mass constituting between 5% and 75% by weight of the oxygen carrier solid, the redox active mass comprising at least one copper oxide and being capable of transporting oxygen in the chemical looping redox combustion process;
a ceramic matrix within which the redox active mass is dispersed, the ceramic matrix constituting between 25% and 95% by weight of the oxygen carrier solid, the ceramic matrix comprising 100% by weight of at least one oxide having a melting point above 1500° C.;
a porosity such that:
the total pore volume of the oxygen carrier solid, measured by mercury porosimetry, is between 0.05 and 1.2 ml/g,
the pore volume of macropores constitutes at least 40% of the total pore volume of the oxygen carrier solid;
the size distribution of the macropores within the oxygen carrier solid, measured by mercury porosimetry, is between 50 nm and 7 μm.

2. The oxygen carrier solid as claimed in claim 1 , wherein the total pore volume of the oxygen carrier solid is between 0.1 and 0.85 ml/g.

3. The oxygen carrier solid as claimed in claim 1 , wherein the size distribution of the macropores within the oxygen carrier solid is between 50 nm and 3 μm.

4. The oxygen carrier solid as claimed in claim 1 , wherein the at least one oxide of the ceramic matrix has a melting point above 1700° C.

5. The oxygen carrier solid as claimed in claim 1 , wherein the at least one oxide of the ceramic matrix comprises at least one selected from the group consisting of calcium aluminate of formula CaAl 2 O 4 , silica of formula SiO 2 , titanium dioxide of formula TiO 2 , perovskite of formula CaTiO 3 , alumina of formula Al 2 O 3 , zirconia of formula ZrO 2 , yttrium dioxide of formula Y 2 O 3 , barium zirconate of formula BaZrO 3 , magnesium aluminate of formula MgAl 2 O 4 , magnesium silicate of formula MgSi 2 O 4 and lanthanum oxide of formula La 2 O 3 .

6. The oxygen carrier solid as claimed in claim 5 , wherein the at least one oxide of the ceramic matrix comprises silica, alumina, or a mixture of alumina and silica.

7. The oxygen carrier solid as claimed in claim 1 , wherein the particles have a particle size such that more than 90% of the particles have a size between 50 μm and 600 μm.

8. A process for preparing an oxygen carrier solid as claimed in claim 1 , comprising:
(A) preparing an aqueous suspension comprising the at least one oxide having a melting point above 1500° C. as a precursor of the ceramic matrix, the at least one oxide forming grains having a size between 0.1 μm and 20 μm;
(B) spray drying the suspension obtained in (A) in order to form particles, the spray drying comprising spraying the suspension in a drying chamber in order to form droplets, and simultaneously bringing the droplets into contact with a hot carrier gas brought to a temperature between 200° C. and 350° C.;
(C) calcining the particles from the spray drying in (B), the calcining being carried out in air and at a temperature between 400° C. and 1400° C.;
(D) optional screening of the calcined particles from (C), by separation using a cyclone;
(E) integrating a redox active mass according to e1) or e2) in order to produce the oxygen carrier solid in the form of particles:
e1) (i) impregnating the particles from (C) with a precursor compound of a redox active mass, then (ii) drying the impregnated particles followed (iii) by a calcination;
e2) incorporating the redox active mass during the preparation of the suspension in (A).

9. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein e1) comprises:
(i) impregnating the particles from (C) with an aqueous or organic solution containing at least one soluble precursor compound of copper.

10. The process for preparing an oxygen carrier solid as claimed claim 9 , wherein the impregnation (i) in e1) is carried out in one or more successive steps.

11. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein the drying (ii) in e1) is carried out in air or in a controlled atmosphere, at a temperature between 30° C. and 200° C.

12. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein the calcining (iii) in e1) is carried out in air at a calcining temperature between 450° C. and 1400° C., and is carried out for a period of 1 to 24 hours.

13. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein e2) comprises (j) impregnating the grains of the at least one oxide as the precursor of the ceramic matrix with an aqueous or organic solution containing at least one soluble precursor compound of copper, the impregnation being carried out before the grains are suspended.

14. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein e2) comprises (jj) adding at least one precursor of the redox active mass to the suspension prepared in (A), the at least one precursor of the redox active mass being a soluble compound of copper.

15. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein e2) comprises (jjj) adding, to the suspension prepared in (A), grains of at least one copper oxide, the grains having a size between 0.1 μm and 20 μm in order to form the redox active mass of the oxygen carrier solid.

16. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein, in A), at least one binder is added to the aqueous suspension, the binder being an organic binder or in inorganic binder.

17. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein, in (A), at least one pore-forming agent is added to the aqueous suspension.

18. The process for preparing an oxygen carrier solid as claimed in claim 8 , wherein fines of the oxygen carrier solid that are produced during the use of the oxygen carrier solid in a process for chemical looping redox combustion of a hydrocarbon feedstock are recycled to (E).

19. A process for chemical looping redox combustion of a hydrocarbon feedstock using an oxygen carrier solid as claimed in claim 1 .

20. The process for chemical looping redox combustion of a hydrocarbon feedstock as claimed in claim 19 , wherein the oxygen carrier solid circulates between at least one reduction zone and an oxidation zone both operating in a fluidized bed, the temperature in the at least one reduction zone and in the oxidation zone being between 400° C. and 1400° C.

21. A process for chemical looping redox combustion of a hydrocarbon feedstock comprising contacting the feedstock with the oxygen carrier solid prepared according to the process as claimed in claim 8 .

22. The oxygen carrier solid as claimed in claim 1 , wherein the at least one oxide of the ceramic matrix has a melting point above 2000° C.

23. The oxygen carrier solid as claimed in claim 5 , wherein the at least one oxide of the ceramic matrix comprises alumina.

Assignees

• Ifp Energies Now
• Total Raffinage Chimie

Inventors

• Lambert Arnold
• Michau Mathieu
• MARTI Delphine
• Comte Elodie

Classifications

• B01J2235/30

  Scanning electron microscopy; Transmission electron microscopy · CPC title

• B01J35/51

  Spheres · CPC title

• B01J35/45

  Nanoparticles · CPC title

• B01J35/31

  Density · CPC title

• B01J2235/15

  X-ray diffraction · CPC title