Catalyst compositions having enhanced acidity for dry reforming processes

Patent metadata

Field	Value
Publication number	US-11478777-B2
Application number	US-202016775135-A
Country	US
Kind code	B2
Filing date	Jan 28, 2020
Priority date	Jan 28, 2020
Publication date	Oct 25, 2022
Grant date	Oct 25, 2022

Abstract

Modified red mud catalyst compositions, methods for production, and methods for use, a composition including red mud material produced from an alumina extraction process from bauxite ore; nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition; and a Periodic Table Group VIB metal oxide, the Group VIB metal oxide present at between about 1 wt. % and about 30 wt. % of the modified red mud catalyst composition.

First claim

That claimed is:

1. A modified red mud catalyst composition, the modified red mud catalyst composition consisting of:
red mud material produced from an alumina extraction process from bauxite ore, where the red mud material comprises aluminum oxide, calcium oxide, iron oxide, sodium oxide, silicon oxide, and titanium oxide such that the modified red mud catalyst composition includes between about 15 wt. % and about 30 wt. % Al 2 O 3 , between about 1 wt. % and about 5 wt. % CaO, between about 10 wt. % and about 30 wt. % Fe 2 O 3 , between about 1 wt. % and about 5 wt. % Na 2 O,

between about 10 wt. % and about 25 wt. % SiO 2 , and between about 1 wt. % and about 10 wt. % TiO 2 ;
nickel oxide, the nickel oxide present at between about 15 wt. % to about 25 wt. % of the modified red mud catalyst composition; and
a Periodic Table Group VIB metal oxide, the Group VIB metal oxide present at between about 1 wt. % and about 30 wt. % of the modified red mud catalyst composition, where the Group VIB metal oxide comprises at least one metal selected from the group consisting of: chromium, molybdenum, and tungsten.

2. The modified red mud catalyst according to claim 1 , where the modified red mud catalyst composition comprises particles having a particle size of less than about 70 μm.

3. The modified red mud catalyst composition according to claim 1 , where the nickel oxide is present at about 23 wt. % of the modified red mud catalyst composition.

4. The modified red mud catalyst composition according to claim 1 , where the Group VIB metal oxide is present at between about 1 wt. % to about 20 wt. % of the modified red mud catalyst composition.

5. The modified red mud catalyst composition according to claim 1 , where the Group VIB metal oxide is present at between about 1 wt. % to about 10 wt. % of the modified red mud catalyst composition.

6. The modified red mud catalyst composition according to claim 1 , where the Group VIB metal oxide is present at about 5 wt. % of the modified red mud catalyst composition.

7. The modified red mud catalyst composition according to claim 1 , where Brunauer-Emmett-Teller (BET) surface area of the modified red mud catalyst composition is between about 50 m 2 /g and about 90 m 2 /g.

8. A method for producing the modified red mud catalyst composition of claim 1 , the method comprising the steps of:
a) dissolving red mud material produced from an alumina extraction process from bauxite ore in water to produce a red mud solution;
b) neutralizing the pH of the red mud solution using an acid;
c) preparing a nickel-containing solution, where the nickel-containing solution consists of nickel nitrate dissolved in ethanol;
d) preparing a Periodic Table Group VIB metal oxide-containing solution, where the Group VIB metal oxide comprises at least one metal selected from the group consisting of: chromium, molybdenum, and tungsten;
e) mixing the red mud solution, the nickel-containing solution, and the Group VIB metal oxide-containing solution to precipitate the modified red mud catalyst composition; and
f) calcining the modified red mud catalyst composition,
wherein the modified red mud catalyst composition provides constant methane conversion above about 13% between 1 hour and 6 hours and provides hydrogen production above 8% between 1 hour and 6 hours in dry reforming processes at molar ratios of CH 4 to CO 2 between about 1:1 and about 1:1.75.

9. The method according to claim 8 , where the water comprises deionized water.

10. The method according to claim 8 , where the acid comprises hydrochloric acid.

11. The method according to claim 8 , where the Group VIB metal oxide-containing solution comprises ammonium molybdate dissolved in ethanol.

12. The method according to claim 8 , further comprising filtering the modified red mud catalyst composition and drying the modified red mud catalyst composition before the step of calcining.

13. The method according to claim 12 , where the step of drying occurs at about 100° C.

14. The method according to claim 8 , where the step of calcining takes place for about 4 hours at between about 500° C. to about 700° C.

15. The method according to claim 8 , where the step of calcining takes place for about 4 hours at about 600° C.

16. The method according to claim 8 , further comprising the step of grinding the modified red mud catalyst composition to a particle size of less than about 70 μm.

17. The method according to claim 8 , where Brunauer-Emmett-Teller (BET) surface area of the modified red mud catalyst composition is between about 50 m 2 /g and about 90 m 2 /g.

18. A method for dry reforming over a modified red mud catalyst composition, the method comprising the steps of:
providing a methane feed and carbon dioxide feed to react over the modified red mud catalyst composition at a temperature between about 500° C. to about 1000° C. and a pressure between about 5 bar and about 20 bar to produce synthesis gas comprising H 2 and CO, the modified red mud catalyst composition consisting of:
red mud material produced from an alumina extraction process from bauxite ore where the red mud material comprises aluminum oxide, calcium oxide, iron oxide, sodium oxide, silicon oxide, and titanium oxide such that the modified red mud catalyst composition includes between about 15 wt. % and about 30 wt. % Al 2 O 3 , between about 1 wt. % and about 5 wt. % CaO, between about 10 wt. % and about 30 wt. % Fe 2 O 3 , between about 1 wt. % and about 5 wt. % Na 2 O,

between about 10 wt. % and about 25 wt. % SiO 2 , and between about 1 wt. % and about 10 wt. % TiO 2 ;
nickel oxide, the nickel oxide present at between about 15 wt. % to about 25 wt. % of the modified red mud catalyst composition; and
a Periodic Table Group VIB metal oxide, the Group VIB metal oxide present at between about 1 wt. % and about 30 wt. % of the modified red mud catalyst composition, where the Group VIB metal oxide comprises at least one metal selected from the group consisting of: chromium, molybdenum, and tungsten.

19. The method according to claim 18 , where the Group VIB metal oxide comprises at least one metal selected from the group consisting of: chromium, molybdenum, and tungsten.

20. The method according to claim 18 , where the temperature is between about 600° C. to about 800° C.

21. The method according to claim 18 , where the temperature is about 750° C.

22. The method according to claim 18 , where the pressure is between about 10 bar and about 15 bar.

23. The method according to claim 18 , where the pressure is about 14 bar.

24. The method according to claim 18 , where the methane conversion rate is at least about 14% for at least about 6 hours.

25. The method according to claim 18 , where the modified red mud catalyst composition comprises particles with a particle size of less than about 70 μm.

26. The method according to claim 18 , where the nickel oxide is present at about 23 wt. % of the modified red mud catalyst composition.

27. The method according to claim 18 , where the Group VIB metal oxide is present at between about 1 wt. % to about 20 wt. % of the modified red mud catalyst composition.

28. The method according to claim 18 , where the Group VIB metal oxide is present at between about 1 wt. % to about 10 wt. % of the modified red mud catalyst composition.

29. The method according to cl

Assignees

• Saudi Arabian Oil Co

Inventors

• Alsolami Bandar H
• Fadhel Bandar A
• Bamagain Rami
• Albuali Mohammed A

Classifications

• C01B3/384 Primary

  with external heating of the catalyst · CPC title

• B01J37/088

  Decomposition of a metal salt · CPC title

• B01J23/883

  and nickel · CPC title

• B01J37/035

  Precipitation on carriers · CPC title

• C01B2203/1082

  Composition of support materials · CPC title