IP Library Granted Patent US 11,865,519
Granted Patent B2
US 11,865,519 · App. 17/273,108 · Granted Jan 9, 2024

Noble metal-promoted IN2O3 catalyst for the hydrogenation of CO2 to methanol

Inventors: Joseph Stewart (Uccle, BE); Daniel Curulla-Ferre (Uccle, BE); Javier Perez-Ramirez (Zürich, CH); Cecilia Mondelli (Zürich, CH); Matthias Frei (Zürich, CH)
Assignees: TOTAL SE; ETH ZURICH
B01J23/62B01J6/001B01J21/066B01J23/08B01J23/42B01J23/44B01J35/006B01J35/023B01J35/1014B01J35/1019B01J37/0201B01J37/031C07C1/043C07C1/046C07C29/157
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Quick Facts
Patent No.
US 11,865,519
App. No.
17/273,108
Granted
Jan 9, 2024
Kind
B2
Abstract

Method to prepare a catalyst for use in a process for the synthesis of methanol, comprising indium oxide in the form of In 2 O 3 , and at least one additional metal selected from a noble metal; and in that the average particle size of said noble metal phase is, preferably at least 0.05 nm, and less than 5 nm as determined by STEM-EDX, characterized in that the catalyst is prepared by co-precipitation of a saline solution at a pH above 8.5 comprising an indium salt and a salt of the at least one additional metal selected from a noble metal and optionally further comprising a salt of the at least one alkaline earth metal.

Claims (11)

1. A Method to prepare a catalyst for use in a process for the synthesis of methanol, comprising indium oxide in the form of In 2 O 3 , and at least one additional metal selected from a noble metal; and in that the average particle size of said noble metal phase is, at least 0.05 nm, and less than 5 nm as determined by STEM-EDX, characterized in that the catalyst is prepared by co-precipitation of a saline solution at a pH above 8.5 comprising an indium salt and a salt of the at least one additional metal selected from a noble metal and optionally further comprising a salt of the at least one alkaline earth metal; comprising a further calcination step of the catalyst, wherein the calcined catalyst obtained comprised from 0.01 to 1.0 wt. % of the additional noble metal based on the total weight of the calcined catalyst and wherein the catalyst content of indium oxide in the form of In 2 O 3 based on the calcined catalyst is ranging from 60 to 99.99 wt. %.

2. The method according to claim 1 , characterized in that the co-precipitation is performed at a pH above 9; and at a temperature of at least 293 K (19.85° C.).

3. The method according to claim 1 , characterized in that the catalyst is a calcined catalyst, and in that the method comprises a step of calcination of the catalyst performed at a temperature of at least 473 K (199.85° C.).

4. The method according to claim 1 , characterized in that said catalyst further comprises at least one alkaline earth metal.

5. The method according to claim 1 , characterized in that said catalyst further comprises at least one alkaline earth metal being incorporated simultaneously with said indium salt and a said salt of the at least one additional metal selected from a noble metal at the co-precipitation stage.

6. The method according to claim 1 characterized in that said In 2 O 3 is present in the form of particles having an average crystal size of less than 20 nm as determined by XRD.

7. The method according to claim 1 characterized in that said In 2 O 3 is present in the form of particles having an average crystal size of less than 10 nm as determined by XRD.

8. The method according to claim 1 , characterized in that said at least one additional metal is a noble metal selected from ruthenium (Ru), rhodium (Rh), palladium (Pd), silver (Ag), osmium (Os), platinum (Pt), copper (Cu), gold (Au), iridium (Ir), and any combination thereof.

9. The method according to claim 1 , characterized in that said at least one additional metal is a noble metal selected palladium (Pd) and/or platinum (Pt).

10. The method according to claim 1 , characterized in that the average particle size of the noble metal phase obtained on said catalyst is less than 4 nm as determined by STEM-EDX.

11. The method according to claim 1 , characterized in that the average particle size of the noble metal phase obtained on said catalyst is less than 2 nm as determined by STEM-EDX.

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE NAME OF THE ASSIGNEE PREVIOUSLY RECORDED AT REEL: 67096 FRAME: 87. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Jun 26, 2024
From: TOTALENERGIES SE (PREVIOUSLY TOTAL SA THEN TOTAL SE)
To: TOTALENERGIES ONETECH
Reel/Frame 068051/0530 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 12, 2024
From: TOTALENERGIES SE (PREVIOUSLY TOTAL SA THEN TOTAL SE)
To: TOTALENERGIES ONETECH (PREVIOUSLY TOTALENERGIES ONE TECH)
Reel/Frame 067096/0087 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 13, 2021
From: STEWART, JOSEPH; CURULLA-FERRE, DANIEL; PEREZ-RAMIREZ, JAVIER; MONDELLI, CECILIA; FREI, MATTHIAS
To: TOTAL SE; ETH ZURICH
Reel/Frame 055906/0127 →
Priority Claims (2)
EP 18306174 · Sep 6, 2018 · regional
EP 18306175 · Sep 6, 2018 · regional
Continuity (1)
Related Publication 20210354114A1 · Nov 18, 2021