Catalyst for use in catalytic oxidation or ammoxidation of propane or isobutane in the gaseous phase

• US 7,087,551 B2
• Filed: 08/30/2002
• Issued: 08/08/2006
• Est. Priority Date: 06/15/2000
• Status: Expired due to Term

• Current Assignee: Asahi Kasei Kabushiki Kaisha (Asahi Kasei Corporation)
• Original Assignee: Asahi Kasei Kabushiki Kaisha (Asahi Kasei Corporation)
• Inventors: Watanabe, Mamoru, Komada, Satoru, Hinago, Hidenori, Nagano, Osamu
• Primary Examiner(s): Richter, Johann
• Assistant Examiner(s): SACKEY, EBENEZER O
• Application Number:
  US10/231,113
• Publication Number:
  US 20030088118A1
• Time in Patent Office: 1,439 Days
• Field of Search: 558/321, 558/318, 558/319, 502/215, 502/309, 502/211, 502/321
• US Class Current: 502/211
• CPC Class Codes: B01J 23/002 Mixed oxides other than spinels, e.g. perovskite
• CPC Class Codes: B01J 23/18 Arsenic, antimony or bismuth
• CPC Class Codes: B01J 23/20 Vanadium, niobium or tantalum
• CPC Class Codes: B01J 23/28 Molybdenum
• CPC Class Codes: B01J 23/8877 Vanadium, tantalum, niobium or polonium
• CPC Class Codes: B01J 2523/00 Constitutive chemical elements of heterogeneous catalysts
• CPC Class Codes: B01J 2523/31 Aluminium
• CPC Class Codes: B01J 2523/41 Silicon
• CPC Class Codes: B01J 2523/43 Tin
• CPC Class Codes: B01J 2523/47 Titanium
• CPC Class Codes: B01J 2523/53 Antimony
• CPC Class Codes: B01J 2523/55 Vanadium
• CPC Class Codes: B01J 2523/56 Niobium
• CPC Class Codes: B01J 2523/64 Tellurium
• CPC Class Codes: B01J 2523/68 Molybdenum
• CPC Class Codes: B01J 2523/69 Tungsten
• CPC Class Codes: B01J 2523/842 Iron
• CPC Class Codes: B01J 27/0576 Tellurium; Compounds thereof
• CPC Class Codes: C07C 253/24 by ammoxidation of hydrocarbons or substituted hydrocarbons
• CPC Class Codes: C07C 255/08 Acrylonitrile; Methacrylonitrile
• CPC Class Codes: C07C 51/215 : of saturated hydrocarbyl groups
• CPC Class Codes: C07C 57/04 : Acrylic acid; Methacrylic acid
• CPC Class Codes: Y02P 20/52 : using catalysts, e.g. selective catalysts

Abstract

Disclosed is an oxide catalyst comprising an oxide represented by the formula Mo₁V_aNb_bX_cY_dZ_eQ_fO_n (wherein: X is at least one element selected from the group consisting of Te and Sb; Y is at least one element selected from the group consisting of Al and W; Z is at least one element selected from the group consisting of elements which individually form an oxide having a rutile structure and a Z oxide having a rutile structure is used as a source of Z for producing the catalyst; Q is at least one element selected from the group consisting of titanium, tin, germanium, lead, tantalum, ruthenium, rhenium, rhodium, iridium, platinum, chromium, manganese, technetium, osmium, iron, arsenic, cerium, cobalt, magnesium, nickel and zinc, and a Q compound not having a rutile structure is used as a source of Q for producing the catalyst; and a, b, c, d, e, f and n are, respectively, the atomic ratios of V, Nb, X, Y, Z, Q and O, relative to Mo). Also disclosed is a process for producing an unsaturated carboxylic acid or an unsaturated nitrile by using the above-mentioned oxide catalyst.

Claims

1. An oxide catalyst for use in catalytic oxidation or ammoxidation of propane or isobutane in the gaseous phase, which comprises an oxide represented by the following formula (I):

Mo₁V_aNb_bX_cY_dZ_eQ_fO_n 

 

(I)

wherein;

X is at least one element selected from the group consisting of tellurium and antimony;

Y is at least one element selected from the group consisting of aluminum and tungsten;

Z is at least one element selected from the group consisting of elements which individually form an oxide having a rutile structure and which are titanium, tin, germanium, lead, tantalum, ruthenium, rhenium, rhodium, iridium, platinum, molybdenum, vanadium, niobium, tellurium, antimony, aluminums and tungsten;

Q is at least one element selected from the group consisting of titanium, tin, germanium, lead, tantalum, ruthenium, rhenium, rhodium, iridium, platinum, chromium, manganese, technetium, osmium, iron, arsenic, cerium, cobalt, magnesium, nickel and zinc; and

a, b, c, d, e, f and n are, respectively, the atomic ratios of vanadium (V), niobium (Nb), X, Y, Z, Q and oxygen (O), relative to molybdenum (Mo),

wherein;

0.1≦

a≦

1.0,

0.01≦

b≦

1.0,

0.01≦

c≦

1.0,

0≦

d≦

5,

0≦

e≦

3,

0≦

f≦

9,

with the proviso that 0<

d+e≦

3.5, and

n is a number determined by and consistent with the valence requirements of the

other elements present in the oxide of formula (I);

said oxide catalyst being produced by calcining a dried catalyst precursor, said precursor comprising;

(i) a molybdenum (Mo) compound which does not have a rutile structure;

(ii) a vanadium (V) compound which does not have a rutile structure;

(iii) a niobium (Nb) compound which does not have a rutile structure;

(iv) at least one X compound selected from the group consisting of compounds of elements defined as X in formula (I), wherein said X compound does not have a rutile structure;

(v) at least one compound selected from the group consisting of the following compounds (v-1) and (v-2);

(v-1) at least one Y compound selected from the group consisting of compounds of elements defined as Y in formula (I), wherein said Y compound does not have a rutile structure, and

(v-2) at least one Z oxide selected from the group consisting of oxides of elements defined as Z in formula (I), wherein said Z oxide has a rutile structure; and

optionally

(vi) at least one Q compound selected from the group consisting of compounds of elements defined as Q in formula (I), wherein said Q compound does not have a rutile structure,

wherein said Mo compound, said V compound, said Nb compound, said X compound, said Y compound, said Z oxide and said Q compound are, respectively, used in amounts such that the atomic ratios of the Mo, V, Nb, X, Y, Z and Q in the catalyst obtained satisfy the atomic ratio requirements defined for formula (I).

2. The oxide catalyst according to claim 1, wherein X in formula (I) is antimony.

3. The oxide catalyst according to claim 1, wherein Y in formula (I) is aluminum and said compound (v-1) is aluminum oxide.

4. The oxide catalyst according to claim 1, wherein Z in formula (I) is at least one element selected from the group consisting of titanium and tin.

5. The oxide catalyst according to claim 1, which further comprises a silica carrier having supported thereon said oxide, wherein said silica carrier is present in an amount of from 20 to 60% by weight in terms of SiO₂, based on the total weight of said oxide and said silica carrier in terms of SiO₂.

6. The oxide catalyst according to claim 1, wherein said dried catalyst precursor further comprises a dicarboxylate value.

7. The oxide catalyst according to claim 1, wherein the calcination is performed in an inert gas atmosphere which is substantially free from molecular oxygen.

8. The oxide catalyst according to claim 1, wherein said dried catalyst precursor is produced by a method comprising the following steps (1) and (2):

(1) providing a solution or slurry of a raw material mixture in an aqueous medium, said raw material mixture comprising said compounds (i) to (vi); and

(2) drying said raw material mixture solution or slurry obtained in step (1), to thereby obtain said dried catalyst precursor.

9. The oxide catalyst according to claim 8, wherein, in step (1) of providing said raw material mixture solution or slurry, said niobium compound (iii) is used in the form of a niobium-containing aqueous solution comprising water having dissolved therein a dicarboxylic acid and said niobium compound (iii), wherein the molar ratio of said dicarboxylic acid to said niobium compound (iii) in terms of niobium is from 1 to 8.

10. The oxide catalyst according to claim 9, wherein said niobium-containing aqueous solution further comprises hydrogen peroxide, wherein the molar ratio of said hydrogen peroxide to said niobium compound (iii) in terms of niobium is from 0.5 to 10.

11. A process for producing acrylic acid or methacrylic acid, which comprises reacting propane or isobutane with molecular oxygen in the gaseous phase in the presence of the oxide catalyst of claim 1.

12. A process for producing acrylonitrile or methacrylonitrile, which comprises reacting propane or isobutane with ammonia and molecular oxygen in a gaseous phase in the presence of an oxide catalyst which comprises an oxide represented by the following formula (I):

Mo₁Y_aNb_bX_cY_dZ_eQ_fO_n 

 

(I)

wherein;

X is at least one element selected from the group consisting of tellurium and antimony;

Y is at least one element selected from the group consisting of aluminum and tungsten;

Z is at least one element selected from the group consisting of elements which individually form an oxide having a rutile structure and which are titanium, tin, germanium, lead, tantalum, ruthenium, rhenium, rhodium, iridium, platinum, molybdenum, vanadium, niobium, tellurium, antimony, aluminum and tungsten;

Q is at least one element selected from the group consisting of titanium, tin, germanium, lead, tantalum, ruthenium, rhenium, rhodium, iridium, platinum, chromium, manganese, technetium, osmium, iron, arsenic, cerium, cobalt, magnesium, nickel and zinc; and

a, b, c, d, e, f and n are, respectively, the atomic ratios of vanadium (V), niobium (Nb), X, Y, Z, Q and oxygen (O), relative to molybdenum (Mo),

wherein;

0.1≦

a≦

1.0,

0.01≦

b≦

1.0,

0.01≦

c≦

1.0,

0≦

d≦

0.5,

0≦

e≦

3,

0≦

f≦

9,

with the proviso that 0<

d+e≦

3.5, and

n is a number determined by and consistent with the valence requirements of the other elements present in the oxide of formula (I);

said oxide catalyst being produced by calcining a dried catalyst precursor, said precursor comprising;

(i) a molybdenum (Mo) compound which does not have a rutile structure;

(ii) a vanadium (V) compound which does not have a rutile structure;

(iii) a niobium (Nb) compound which does not have a rutile structure;

(iv) at least one X compound selected from the group consisting of compounds of elements defined as X in formula (I), wherein said X compound does not have a rutile structure;

(v) at least one compound selected from the group consisting of the following compounds (v-1) and (v-2);

(v-1) at least one Y compound selected from the group consisting of compounds of elements defined as Y in formula (I), wherein said Y compound does not have a rutile structure, and

(v-2) at least one Z oxide selected from the group consisting of oxides of elements defined as Z in formula (I), wherein said Z oxide has a rutile structure; and

optionally

(vi) at least one Q compound selected from the group consisting of compounds of elements defined as Q in formula (I), wherein said Q compound does not have a rutile structure,

wherein said Mo compound, said V compound, said Nb compound, said X compound, said Y compound, said Z oxide and said Q compound are, respectively, used in amounts such that the atomic ratios of the Mo, V, Nb, X, Y, Z and Q in the catalyst obtained satisfy the atomic ratio requirements defined for formula (I).