IP Library Granted Patent US 11,260,371
Granted Patent B2
US 11,260,371 · App. 16/062,242 · Granted Mar 1, 2022

Selective catalytic reduction (SCR) catalyst comprising a composite oxide containing V and SB, preparation process thereof, and use thereof for nitrogen oxides removal

Inventors: Feng Zhao (Shanghai, CN); Jia Di Zhang (Shanghai, CN); Liang Chen (Shanghai, CN); Diana Carolina Galeano Nunez (Ludwigshafen, DE); Sabine Huber (Ludwigshafen, DE); Edgar Viktor Huennekes (Hannover, DE)
Assignee: BASF CORPORATION
B01J23/22B01D53/8628B01D53/9418B01J23/002B01J35/002B01J37/0009B01J37/0215B01J37/0236B01J37/03B01J37/04B01J37/08B01D2251/2062B01D2255/2098B01D2255/20707B01D2255/20723B01D2255/30B01D2255/40B01J21/063B01J35/026B01J37/031B01J2523/00
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Quick Facts
Patent No.
US 11,260,371
App. No.
16/062,242
Granted
Mar 1, 2022
Kind
B2
Abstract

A catalyst composition comprising—a support comprising TiO 2 ,—a composite oxide containing vanadium and antimony, which has a rutile-type structure different from VSbO 4 and V 0.92 Sb 0.92 O 4 as determined by X-ray diffraction (XRD) analysis with CuKα radiation, and—optionally, one or more selected from the group consisting of oxides of silicon, oxides of vanadium and oxides of antimony, for selective catalytic reduction of nitrogen oxides; to a process for preparing the catalyst composition, to the catalyst composition obtained/obtainable by the process and to use of the same for selective catalytic reduction of nitrogen oxides.

Claims (33)

1. A catalyst composition comprising:

a support comprising TiO 2 ,

a composite oxide containing vanadium and antimony, which has a rutile-base structure different from VSbO 4 and V 0.92 Sb 0.92 O 4 as determined by X-ray diffraction (XRD) analysis with Cu Kα radiation, and

optionally, one or more selected from the group consisting of oxides of silicon, oxides of vanadium, and oxides of antimony,

wherein the catalyst composition is capable of selective catalytic reduction of nitrogen oxides.

2. The catalyst composition according to claim 1 , wherein the composite oxide containing vanadium and antimony is characterized by an XRD diffraction peak of (110) or (101) plane at higher 2θ than those of VSbO 4 and V 0.92 Sb 0.92 O 4 by at least 0.1°.

3. The catalyst composition according to claim 2 , wherein the composite oxide containing vanadium and antimony is characterized by an XRD diffraction peak of (101) plane at higher 2θ than those of VSbO 4 and V 0.92 Sb 0.92 O 4 by at least 0.2°.

4. The catalyst composition according to claim 3 , wherein the composite oxide containing vanadium and antimony is characterized by an XRD diffraction peak of (101) plane at higher 20 than those of VSbO 4 and V 0.92 Sb 0.92 O 4 by at least 0.5°.

5. The catalyst composition according to claim 1 , wherein the composite oxide containing vanadium and antimony is characterized by an XRD diffraction peak of (110) plane at 2θ in the range of from 27.25° to 29.00° and an XRD diffraction peak of (101) plane at 2θ in the range of from 35.43° to 37.00°.

6. The catalyst composition according to claim 1 , wherein vanadium, including those in both the composite oxide containing vanadium and antimony and the optional oxides of vanadium, is present in the catalyst composition in the range of 0.5% to 6% by weight, calculated as elemental V; and wherein antimony, including those in both the composite oxide containing vanadium and antimony and the optional oxides of antimony, is present in the catalyst composition in the range of 0.8% to 16% by weight, calculated as elemental Sb.

7. The catalyst composition according to claim 6 , wherein vanadium, including those in both the composite oxide containing vanadium and antimony and the optional oxides of vanadium, is present in the catalyst composition in the range of 1% to 4.5% by weight, calculated as elemental V.

8. The catalyst composition according to claim 6 , wherein vanadium, including those in both the composite oxide containing vanadium and antimony and the optional oxides of vanadium, is present in the catalyst composition in the range of 2% to 4% by weight, calculated as elemental V.

9. The catalyst composition according to claim 6 , wherein antimony, including those in both the composite oxide containing vanadium and antimony and the optional oxides of antimony, is present in the catalyst composition in the range of 3.5% to 14% by weight, calculated as elemental Sb.

10. The catalyst composition according to claim 6 , wherein antimony, including those in both the composite oxide containing vanadium and antimony and the optional oxides of antimony, is present in the catalyst composition in the range of 5% to 10% by weight, calculated as elemental Sb.

11. The catalyst composition according to claim 1 , wherein the catalyst composition is in a shaped form or is carried on a substrate.

12. The catalyst composition according to claim 11 , wherein the catalyst composition is in the shaped form of extrudate.

13. The catalyst composition according to claim 1 , wherein the nitrogen oxides are present in exhaust gases from an internal combustion engine, a power plant, or an incinerator.

14. The catalyst composition according to claim 13 , wherein the internal combustion engine is a diesel engine.

15. A process for preparing the catalyst composition as defined in claim 1 , which includes steps of:

(i) mixing a vanadium/antimony oxide and optionally a silicon source with the support comprising TiO 2 in a solvent to obtain a suspension;

(ii) optionally, applying the suspension onto a substrate;

(iii) drying at a temperature in the range of 80 and 250° C.; and

(iv) calcining at a temperature of at least 500° C.

16. The process according to claim 15 , wherein the calcining in step (iv) is conducted at a temperature in the range of 500° C. to 700° C.

17. The process according to claim 16 , wherein the calcining in step (iv) is conducted at a temperature in the range of 550° C. to 700° C.

18. The process according to claim 15 , wherein the vanadium/antimony oxide used in step (i) is prepared by

(a) providing a suspension comprising vanadium oxide and antimony oxide; and

(b) drying the suspension to obtain the vanadium/antimony oxide at a temperature in the range of 80° C. to 250° C.

19. The process according to claim 15 , wherein the vanadium/antimony oxide used in step (i) is prepared by

(a′) providing a suspension or solution comprising a vanadium source and an antimony source;

(b′) precipitating and separating the vanadium/antimony oxide from the suspension or solution; and

(c′) optionally, drying at a temperature in the range of 80° C. to 250° C.

20. The process according to claim 15 , which does not comprise step (ii), and optionally comprises a step of shaping in order to obtain the catalyst composition in a shaped form.

Assignments (8)
NUNC PRO TUNC ASSIGNMENT Recorded Jan 24, 2025
From: BASF SE
To: BASF CATALYSTS LLC
Reel/Frame 070001/0877 →
NUNC PRO TUNC ASSIGNMENT Recorded Jan 24, 2025
From: BASF CATALYSTS LLC
To: BASF MOBILE EMISSIONS CATALYSTS LLC
Reel/Frame 070002/0453 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 3, 2021
From: BASF SE
To: BASF CORPORATION
Reel/Frame 057379/0453 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2018
From: ZHAO, FENG; ZHANG, JIA DI; CHEN, LIANG
To: BASF CATALYSTS (SHANGHAI) CO., LTD
Reel/Frame 046959/0978 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2018
From: HUENNEKES, EDGAR VIKTOR
To: BASF CATALYSTS GERMANY GMBH
Reel/Frame 046960/0342 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2018
From: BASF CATALYSTS GERMANY GMBH
To: BASF CORPORATION
Reel/Frame 046962/0582 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2018
From: BASF CATALYSTS (SHANGHAI) CO., LTD
To: BASF CORPORATION
Reel/Frame 046725/0288 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2018
From: GALEANO NUNEZ, DIANA CAROLINA; HUBER, SABINE
To: BASF SE
Reel/Frame 046725/0986 →
Priority Claims (1)
WO PCT/CN2015/097704 · Dec 17, 2015 · international
Continuity (1)
Related Publication 20180304236A1 · Oct 25, 2018