IP Library Granted Patent US 11,547,989
Granted Patent B2
US 11,547,989 · App. 16/966,638 · Granted Jan 10, 2023

Cored round trilobe shaped catalyst for producing maleic anhydride

Inventors: Chunli Zhao (The Woodlands, TX); Bennie Albert Horrell, Jr. (The Woodlands, TX); William S. Frazee (The Woodlands, TX)
Assignee: Huntsman Petrochemical LLC
B01J35/026B01J27/198B01J35/023B01J35/1014B01J35/1038B01J37/0009B01J37/08C07D307/60B01J2531/56
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Quick Facts
Patent No.
US 11,547,989
App. No.
16/966,638
Granted
Jan 10, 2023
Kind
B2
Abstract

The present disclosure provides an improved shaped catalyst containing catalytic material comprised of mixed oxides of vanadium and phosphorus and using such shaped catalysts for the production of maleic anhydride.

Claims (26)

1. A shaped catalyst for preparing maleic anhydride comprising:

a) a catalytic material comprising mixed oxides of vanadium and phosphorus and;

b) a hollow core; and

c) a first end, a second end and a wall disposed between the first end and the second end, the wall comprising a height and n crenellations running along the height of the wall to form n lobes wherein each lobe has a corner defined by a lobe radius and n is 3, 4 or 5.

2. The shaped catalyst according to claim 1 wherein the crenellations are circular arcs.

3. The shaped catalyst according to claim 2 wherein the wall has three crenellations to form three lobes.

4. The shaped catalyst according to claim 2 wherein the wall has a height ranging from 1 mm to 20 mm.

5. The shaped catalyst according to claim 2 wherein the first end and second end have a diameter ranging from 5 mm to 9 mm.

6. The shaped catalyst according to claim 2 wherein the hollow core has a diameter ranging from 0.5 mm to 4 mm.

7. The shaped catalyst according to claim 2 wherein an inner crenellation feature connecting innermost points of the crenellations has a diameter ranging from 2 mm to 4.5 mm.

8. The shaped catalyst according to claim 2 wherein the lobe radius ranges from 0.375 mm to 0.75 mm.

9. The shaped catalyst according to claim 2 wherein an outer crenellation feature connecting the innermost points and projecting edges of a crenellation has a diameter ranging from 2 mm to 3.5.

10. The shaped catalyst according to claim 2 wherein the shaped catalyst has a three points of contact distance ranging between 4 mm and 8 mm.

11. The shaped catalyst according to claim 10 wherein the shaped catalyst has a two points of contact distance ranging between 5 mm and 10 mm.

12. The shaped catalyst according to claim 5 wherein a ratio of a diameter of the hollow core to the diameter for the first end and the second end is between 0.15 and 0.3.

13. The shaped catalyst according to claim 7 wherein a ratio of a diameter of the hollow core to the diameter of the inner crenellation feature ranges between 0.4 and 0.6.

14. The shaped catalyst according to claim 8 wherein a ratio of a diameter of the hollow core to the lobe radius ranges between 2.8 and 3.2.

15. The shaped catalyst according to claim 2 further wherein the shaped catalyst has a side crush strength of greater than 10 lbs.

16. A method for preparing a shaped catalyst comprising reacting a vanadium-containing compound and a phosphorus-containing compound in an alcoholic medium to produce a VPO catalyst precursor, shaping the VPO catalyst precursor to form the shaped catalyst and activating the shaped catalyst by calcination wherein the shaped catalyst comprises

a) a catalytic material comprising mixed oxides of vanadium and phosphorus and;

b) a hollow core; and

c) a first end, a second end and a wall disposed between the first end and the second end, the wall comprising a height and n crenellations running along the height of the wall to form n lobes wherein each lobe has a corner defined by a lobe radius and n is 3, 4 or 5.

17. The method according to claim 16 wherein the VPO catalyst precursor is shaped by pressing or compacting in a mold.

18. The method of claim 17 wherein the shaped catalyst is subjected to a series of contactings with an organic solvent or a mixture of organic solvents after calcination.

19. A process for preparing maleic anhydride comprising reacting a hydrocarbon having at least four carbons in a straight chain or cyclic ring with a molecular oxygen-containing gas in the presence of a shaped catalyst according to claim 1 .

20. The process according to claim 19 wherein the hydrocarbon having at least four carbons in a straight chain or cyclic ring is selected from n-butane, 1-butene, 2-butene, benzene and a mixture thereof.

Assignments (3)
SECURITY INTEREST Recorded May 4, 2026
From: HUNTSMAN INTERNATIONAL LLC; HUNTSMAN ADVANCED MATERIALS AMERICAS LLC; HUNTSMAN NANOCOMP LLC; HUNTSMAN PETROCHEMICAL LLC
To: CITIBANK N.A.
Reel/Frame 075498/0663 →
PATENT SECURITY AGREEMENT Recorded Mar 10, 2026
From: HUNTSMAN INTERNATIONAL LLC; HUNTSMAN ADVANCED MATERIALS AMERICAS LLC; HUNTSMAN NANOCAMP LLC; HUNTSMAN PETROCHEMICAL LLC
To: CITIBANK, N.A.
Reel/Frame 075106/0238 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 31, 2020
From: ZHAO, CHUNLI; HORRELL, BENNIE ALBERT, JR.; FRAZEE, WILLIAM S.
To: HUNTSMAN PETROCHEMICAL LLC
Reel/Frame 053375/0934 →