IP Library Granted Patent US 8,779,124
Granted Patent B2
US 8,779,124 · App. 13/889,404 · Granted Jul 15, 2014

Ammoximation process

Inventors: Robert Raja (Eastleigh, GB); Alexander James Patterson (Coupar Angus, GB)
Assignee: University of Southampton
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Quick Facts
Patent No.
US 8,779,124
App. No.
13/889,404
Granted
Jul 15, 2014
Kind
B2
Abstract

A redox ammoximation process in which a ketone or aldehyde is reacted with ammonia and oxygen in the presence of a catalyst, wherein: the catalyst is an aluminophosphate based redox catalyst having the qualitative general formula (I) M 1 M 2 AlPO-5 (I) in which M 1 is at least one transition metal atom having redox catalytic capability; M 2 is at least one metal atom in the (IV) oxidation state; M 1 and M 2 are different from each other; and a proportion of the phosphorous atoms in the M 1 M 2 AlPO-5 type structure are replaced by M 2 atoms.

Claims (29)

1. A redox ammoximation process comprising reacting a C 6 -C 12 cyclic ketone with ammonia and oxygen in the presence of a catalyst to form an oxime, wherein:

the catalyst is an aluminophosphate based redox catalyst having the formula (I)

M 1 M 2 AlPO-5  (I)

wherein M 1 is at least one selected from Co(III), Mn(III), Fe(III), Cu(III), V(V), and Ru(III) having redox catalytic capability;

M 2 is at least one selected from Ge(IV), Sn(IV), Ti(IV), and Re(IV); and

a proportion of the phosphorous atoms in the M 1 M 2 AlPO-5 type structure are replaced by M 2 atoms.

2. A process according to claim 1 when M 2 is Ti (IV).

3. A process according to claim 2 wherein the catalyst is selected from Co III Ti IV AlPO-5, Mn III Ti IV Alpo-5, Fe III Ti IV AlPO-5, Cu III Ti IV AlPO-5, V v Ti IV AlPO-5, and Ru III Ti IV AlPO-5.

4. A process according to claim 3 wherein the catalyst is selected from Co III Ti IV AlPO-5, Mn III Ti IV AlPO-5 and Fe III Ti IV AlPO-5.

5. A process according to claim 1 wherein the M 1 is selected from Co(III), Mn(III) and Fe (III).

6. A process according to claim 1 wherein the ammonia is in the form of aqueous ammonium hydroxide.

7. A process according to claim 1 which is carried out at a temperature of from 40 to 200° C.

8. A process according to claim 7 which is carried out at a temperature of from 50 to 90° C.

9. A process according to claim 1 which is carried out at a pressure of from 0.5 MPa [5 bar] to 10 MPa [100 bar].

10. A process according to claim 1 wherein the C 6 -C 12 ketone is cyclohexanone and the oxime is cyclohexanone-oxime.

11. A process of forming an ε-caprolactam comprising reacting cyclohexanone with ammonia and oxygen in the presence of a catalyst to form an cyclohexanone oxime, wherein:

the catalyst is an aluminophosphate based redox catalyst having the formula (I)

M 1 M 2 AlPO-5  (I)

wherein M 1 is at least one selected from Co(III), Mn(III), Fe(III), Cu(III), V(V), and Ru(III) having redox catalytic capability;

M 2 is at least one selected from Ge(IV), Sn(IV), Ti(IV), and Re(IV); and

a proportion of the phosphorous atoms in the M 1 M 2 AlPO-5 type structure are replaced by M 2 atoms; and

converting the oxime to an ε-caprolactam.

12. An aluminophosphate based redox catalyst having the formula (I)

M 1 M 2 AlPO-5  (I)

in which M 1 is at least one selected from Co(III), Mn(III), Fe(III), Cu(III), V(V), and Ru(III) having redox catalytic capability;

M 2 is at least one selected from Ge(IV), Sn(IV), Ti(IV), and Re(IV); and

a proportion of the phosphorous atoms in the M 1 M 2 AlPO-5 type structure are replaced by M 2 atoms.

13. A process according to claim 1 wherein 2 to 18 wt % by weight of the phosphorous atoms in the M 1 M 2 AlPO-5 type structure are replaced by M 2 atoms.

14. A catalyst according to claim 12 wherein 2 to 18 wt % by weight of the phosphorous atoms in the M 1 M 2 AlPO-5 type structure are replaced by M 2 atoms.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 17, 2013
From: RAJA, ROBERT; PATTERSON, ALEXANDER JAMES
To: UNIVERSITY OF SOUTHAMPTON
Reel/Frame 030442/0172 →
Priority Claims (1)
GB 0900198.3 · Jan 7, 2009 · national
Continuity (2)
Continuation 13139930
Related Publication 20130245322A1 · Sep 19, 2013