Olefin metathesis method using a catalyst containing aluminum and molybdenum

Patent metadata

Field	Value
Publication number	US-10322983-B2
Application number	US-201615749344-A
Country	US
Kind code	B2
Filing date	Jul 26, 2016
Priority date	Jul 31, 2015
Publication date	Jun 18, 2019
Grant date	Jun 18, 2019

Abstract

The invention relates to a process for the metathesis of olefins implemented with a catalyst comprising a mesoporous matrix and at least the elements molybdenum and aluminum, said elements being incorporated into said matrix by means of at least one precursor comprising molybdenum and aluminum.

First claim

The invention claimed is:

1. A process for the metathesis of olefins carried out by bringing the olefins into contact with a catalyst comprising a mesoporous matrix and at least the elements molybdenum and aluminium, said elements being incorporated into said matrix using at least one precursor comprising molybdenum and aluminium, in which the catalyst is prepared by dry impregnation according to the process comprising the following stages:
a) solubilization of the precursor comprising molybdenum and aluminium in a volume of solution corresponding to the pore volume of a preformed mesoporous matrix based on oxide,
b) impregnation of the preformed mesoporous matrix based on oxide with the solution obtained in stage a), optional maturation of the solid thus obtained,
c) optional stage of drying, calcination and/or steam treatment of the solid obtained at the end of stage b), in a temperature range from 50° C. to 1000° C., and
d) stage of thermal activation of the solid obtained at the end of stage c), in a temperature range from 100° C. to 1000° C.

2. The process according to claim 1 in which the precursor is a precursor of a heteropolyanion salt, corresponding to formula (I):
(Al a Mo m M b X′ x O y H h ) q− (C r+ ) c .n H 2 O  (I)

in which,
a is greater than 0,
m is greater than or equal to 1,
b is greater than or equal to 0,
x is greater than or equal to 0,
y is greater than or equal to 10,
h is comprised between 0 and 12,
q is comprised between 1 and 20,
r is comprised between 1 and 20,
c is comprised between 1 and 20,
n is comprised between 0 and 200,
x, m, y, h, n and q being integers, M being a metallic element selected from zinc, nickel, cobalt, tungsten, vanadium, niobium, tantalum, iron and copper, and X′ being phosphorus, silicon or boron, and
C represents one or more atoms, identical or different, hydrated or non-hydrated, from the elements of the periodic table capable of existing in cationic form.

3. The process according to claim 2 in which the metallic element M is cobalt, tungsten, or vanadium.

4. The process according to claim 2 in which the precursor of the heteropolyanion salt is an Anderson heteropolyanion salt of formula AlMo 6 O 24 H 6 3− (C r+ ) c .nH 2 O that can also be written as the formula Al(OH) 6 Mo 6 O 18 3− (C r+ ) c .nH 2 O.

5. The process according to claim 4 in which the precursor of the Anderson heteropolyanion salt is [Al(OH) 6 Mo 6 O 18 ] 3− [(C 6 H 10 N 3 O 2 ) 2 Na(H 2 O) 2 ] 3+ 6H 2 O(C 6 H 10 N 3 O 2 =histidinium); [Al(OH) 6 Mo 6 O 18 ] 3− 2 {Na 2 [Me 3 N(CH 2 ) 2 OH] 4 } 6+ .8NH 2 CONH 2 . 4H 2 O; [Al(OH) 6 Mo 6 O 18 ] 3− .(H 3 O + )[Cu(C 6 NO 2 H 4 )(phenantroline)(H 2 O)] + 2 .5H 2 O; [Al(OH) 6 Mo 6 O 18 ] 3− [Al(H 2 O) 6 ] 3+ .10H 2 O, or [Al(OH) 6 Mo 6 O 18 ] 3− [(NH 4 ) + ] 3 .7H 2 O.

6. The process according to claim 2 wherein C is hydrogen, an alkali, or alkaline-earth element, transition metal, a post-transition metal or a rare earth, in hydrated or non-hydrated form, that is an oxygen-containing and/or nitrogen-containing and/or phosphorus-containing organic cation.

7. The process according to claim 6 wherein the cation is an ammonium or phosphonium cation.

8. The process according to claim 1 in which the mesoporous matrix is a matrix based on the oxide of at least one element X that is silicon, titanium, zirconium, magnesium, lanthanum, cerium or mixtures thereof.

9. The process according to claim 1 in which the metathesis reaction is carried out at a temperature comprised between 0 and 500° C.

10. The process according to claim 9 in which the olefins are linear olefins corresponding to formula R 1 R 2 C═CR 3 R 4 , where R 1 , R 2 , R 3 and R 4 , identical or different, are hydrogen or a hydrocarbyl radical of 1 to 20 carbon atoms, or olefins with a cyclic structure, the ring comprising from 3 to 20 carbon atoms.

11. The process according to claim 1 in which the metathesis reaction is the cross-metathesis reaction of ethylene with 2-butene, or the reverse reaction converting propylene to a mixture of ethylene and 2-butene.

12. The process according to claim 1 wherein the pressure in (c) is ≥0.1 MPa.

13. The process according to claim 1 wherein the pressure in (c) is ≤0.1 MPa.

14. The process according to claim 1 wherein the pressure in (d) is ≥0.1 MPa.

15. The process according to claim 1 wherein the pressure in (d) is ≤0.1 MPa.

16. A process for the metathesis of olefins carried out by bringing the olefins into contact with a catalyst comprising a mesoporous matrix and at least the elements molybdenum and aluminium, said elements being incorporated into said matrix using at least one precursor comprising molybdenum and aluminium, in which the catalyst is prepared by impregnation in excess according to the process comprising the following stages:
a′) solubilization of the precursor comprising molybdenum and aluminium in a volume of solution corresponding to between 1.5 and 20 times the pore volume of the preformed mesoporous matrix based on oxide,
b′) impregnation of the preformed mesoporous matrix based on oxide, with the solution obtained in stage a′), filtration and recovery of the solid, optional maturation of the solid thus obtained,
c′) optional stage of drying, calcination and/or steam treatment of the solid obtained at the end of stage b′) in a temperature range from 50° C. to 1000° C., and
d′) stage of thermal activation of the solid obtained at the end of stage c′) in a temperature range from 100° C. to 1000° C.

17. The process according to claim 16 wherein the pressure in (c) is ≥0.1 MPa.

18. The process according to claim 16 wherein the pressure in (c) is ≤0.1 MPa.

19. The process according to claim 16 wherein the pressure in (d) is ≥0.1 MPa.

20. The process according to claim 16 wherein the pressure in (d) is ≤0.1 MPa.

21. A process for the metathesis of olefins carried out by bringing the olefins into contact with a catalyst comprising a mesoporous matrix and at least the elements molybdenum and aluminium, said elements being incorporated into said matrix using at least one precursor comprising molybdenum and aluminium, in which the catalyst is prepared according to the process comprising the following stages:
a1) solubilization of the precursor comprising molybdenum and aluminium and of the precursors of the mesoporous matrix based on oxide of at least one element X in an aqueous or hydro-organic solution in the presence of a pore-forming agent so as to form a colloidal solution,
b1) spray-drying said colloidal solution so as to obtain spherical solid elemental particles incorporating the mesostructured matrix based on oxide and the precursor comprising molybdenum and aluminium,
c1) optional stage of drying, calcination and/or steam treatment of the solid particles obtained at the end of stage b1) and
d1) stage of thermal activation of the dry solid particles at the end of stage c1), in a temperature range from 100 to 1000° C.

22. The process according to claim 21 wherein the pressure in (c) is ≤0.1 MPa.

23. The process according to claim 21 wherein the pressure in (c) is ≥0.1 MPa.

24. The process according to claim 21 wherein the pressure in (d) is ≤0.1 MPa.

25. The process according to claim 21 wherein the pressure in (d) is ≥0.1 MPa.

Assignees

• Ifp Energies Now

Inventors

• Bonduelle Audrey
• Chaumonnot Alexandra
• Delcroix Damien
• Vallee Christophe

Classifications

• C07C11/08

  with four carbon atoms · CPC title

• B01J23/882

  and cobalt · CPC title

• B01J27/19

  Molybdenum · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• B01J21/066

  Zirconium or hafnium; Oxides or hydroxides thereof · CPC title